Nanoplatelet metal hydroxides and methods of preparing same

ABSTRACT

Nanoplatelet forms of metal hydroxide and metal oxide are provided, as well as methods for preparing same. The nanoplatelets are suitable for use as fire retardants and as agents for chemical or biological decontamination.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of U.S. Provisional Application No.60/908,144 filed Mar. 26, 2007; and U.S. Provisional Application No.60/837,791 filed Aug. 11, 2006, the disclosures of which are hereinincorporated by reference in their entirety.

FIELD OF THE INVENTION

Nanoplatelet forms of metal hydroxide and metal oxide are provided, aswell as methods for preparing same. The nanoplatelets are suitable foruse in paper retention, drainage, and opacity, as fire retardants inplastics, rubbers, coatings and textiles and as agents for chemical andbiological preventive and decontamination, in electronics andplasmonics.

BACKGROUND OF THE INVENTION

Metal hydroxides are useful in a variety of applications. For example,magnesium hydroxide (Mg(OH)₂), is employed as flame retardant in variouspolymer compositions. Magnesium hydroxide has advantages over certainother flame retardants in that it is both acid-free and halogen-free.Magnesium hydroxide decomposes endothermically when heated to yieldmagnesium oxide (MgO) and water. The water acts to smother the flame bydiluting and/or excluding oxygen and flammable gases, and a heatinsulating material can form on the surface of certain polymericmaterials containing magnesium hydroxide when in contact with the flame,reducing the availability of potentially flammable decompositionproducts to the gas phase where combustion occurs.

Magnesium oxide is useful as a fireproofing component in constructionmaterials, but has various other uses as well, includinghigh-temperature refractories, electrical insulation, food packaging,cosmetics, fertilizers, and pharmaceuticals

SUMMARY OF THE INVENTION

A method of producing metal hydroxides and metal oxides of superiorproperties is desirable. The materials and methods disclosed herein canbe employed to prepare such metal hydroxides and metal oxides innanoplatelet, nanotube, and other forms. Oxides and hydroxides that canbe prepared according to the preferred embodiments include MgO, SrO,BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, Ni₂O₃, CuO,Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂, Mg(OH)₂, Ca(OH)₂,Al(OH)₃, Sr(OH)₂, Ba(OH)₂, Fe(OH)₃, Cu(OH)₃, Ni(OH)₂, Co(OH)₂, Zn(OH)₂,AgOH, mixed metal oxides, mixed metal hydroxides, and mixtures of metaloxides and hydroxides. The hydroxides and oxides are preferably inplatelet form (e.g., nanoplatelet form), although other configurationscan also be prepared (e.g., tubes such as nanotubes).

In a first aspect, metal hydroxide nanoplatelets are provided, having anaverage platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the first aspect, the metal hydroxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the first aspect, the metal hydroxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the first aspect, the metal hydroxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about −4 mV to about −5 mV.

In an embodiment of the first aspect, the metal hydroxide nanoplateletsare selected from the group consisting of Mg(OH)₂, Ca(OH)₂, Al(OH)₃,Sr(OH)₂, Ba(OH)₂, Fe(OH)₃, Cu(OH)₂, Ni(OH)₂, Co(OH)₂, Zn(OH)₂, AgOH, andmixtures thereof.

In an embodiment of the first aspect, the metal hydroxide nanoplateletsfurther comprise at least one metal oxide. In some embodiments, themetal oxide is selected from the group consisting of MgO, SrO, BaO, CaO,TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, Ni₂O₃, CuO, Al₂O₃, SiO₂,ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂], and mixtures thereof.

In an embodiment of the first aspect, the metal hydroxide nanoplateletsare in a form of rolled nanotubes.

In a second aspect, metal oxide nanoplatelets are provided, having anaverage platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the second aspect, the metal oxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the second aspect, the metal oxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the second aspect, the metal oxide nanoplatelets areselected from the group consisting of MgO, SrO, BaO, CaO, TiO₂, ZrO₂,FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, Ni₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O,[Ce(NO₃)₃—Cu(NO₃)₂]TiO₂, and mixtures thereof.

In a third aspect, a method of producing metal hydroxide nanoplateletsis provided, the method comprising the steps of providing anelectrolyzer comprising an anode compartment, a cathode compartment, anda center compartment situated between the anode compartment and thecathode compartment, and separated from the anode compartment and thecathode compartment by ion selective membranes; adding a solution ofelectrolyte at a pH of about 8 to the anode compartment; adding asolution of up to about 50 wt. % sodium hydroxide at a pH of 8 or higherto the cathode compartment; adding a solution of a second electrolyte tothe center compartment, wherein the solution has from about 30,000 ppmchloride ion to about 200,000 ppm chloride ion; operating the cathodecompartment at an amperage of 3.75 amps per square inch or less, wherebyhydroxide ion is generated in the cathode compartment and migratesthrough its ion selective membrane into the center compartment, andwhereby sodium ion is generated in the anode compartment and migratesthrough its ion selective membrane into the center compartment; andthereafter adding to the center compartment a solution of soluble metalion and a third electrolyte, the solution having from about 300 ppm to100,000 ppm metal ions and from about 5000 ppm to about 200,000 ppmanions, whereby the soluble metal ion reacts with hydroxide ion to yieldmetal hydroxide nanoplatelets, wherein a residence time in the centercompartment of the metal hydroxide nanoplatelets is from about 0.1minutes to about 10 minutes.

In an embodiment of the third aspect, an additional soluble metal ion isadded to the center compartment, wherein the additional soluble metalion is selected from the group consisting of magnesium ion, strontiumion, barium ion, calcium ion, titanium ion, zirconium ion, iron ion,vanadium ion, manganese ion, nickel ion, copper ion, aluminum ion,cobalt ion, silicon ion, zinc ion, silver ion, cerium ion, and mixturesthereof.

In an embodiment of the third aspect, the solution comprises water.

In an embodiment of the third aspect, the solution of soluble metal ionand an electrolyte is adjusted to a pH of 4.5 or less, wherebycarbonates are removed from the solution.

In an embodiment of the third aspect, the solution of soluble metal ionand an electrolyte is added to the center compartment at a temperatureof from about 60° F. to about 190° F.

In an embodiment of the third aspect, the method further comprises thestep of removing residual water from the metal hydroxide nanoplatelets,whereby dried metal hydroxide nanoplatelets are obtained.

In an embodiment of the third aspect, the method further comprises thestep of applying heat to one side of the dried metal hydroxidenanoplatelets, whereby metal hydroxide is converted to metal oxidethrough a portion of a thickness of the nanoplatelets, causing them toroll into nanotubes, whereby metal (hydr)oxide nanotubes are obtained.

In an embodiment of the third aspect, the method further comprises thestep of applying heat to the dried metal hydroxide nanoplatelets,whereby metal hydroxide is converted to metal oxide through thethickness of the nanoplatelets, whereby metal oxide nanoplatelets areobtained.

In an embodiment of the third aspect, the metal hydroxide nanoplateletshave an average platelet diameter of from about 30 nm to about 3500 nmand an average thickness of from about 1 nm to about 400 nm.

In an embodiment of the third aspect, the metal hydroxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the third aspect, the first, second, and thirdelectrolyte is sodium chloride.

In a fourth aspect, magnesium hydroxide nanoplatelets are provided,having an average platelet diameter of from about 30 nm to about 3500 nmand an average thickness of from about 1 nm to about 400 nm.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets have an average platelet diameter of from about 40 nm toabout 120 nm and an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets have an average aspect ratio of from about 15 to about 70,an average BET specific surface area of from about 100 m²/g to about 150m²/g, and an average zeta potential of from about +60 mV to about −60mV.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets have an average aspect ratio of from about 15 to about 70,an average BET specific surface area of from about 100 m²/g to about 150m²/g, and an average zeta potential of from about −4 mV to about −5 mV.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets, further comprise a second metal hydroxide selected fromthe group consisting of Ca(OH)₂, Al(OH)₃, Sr(OH)₂, Ba(OH)₂, Fe(OH)₃,Cu(OH)₂, Ni(OH)₂, Co(OH)₂, Zn(OH)₂, AgOH, and mixtures thereof.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets further comprise at least one metal oxide. In someembodiments, the metal oxide is selected from the group consisting ofMgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO,Ni₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂], and mixturesthereof.

In an embodiment of the fourth aspect, the magnesium hydroxidenanoplatelets are in a form of rolled nanotubes.

In a fifth aspect, magnesium oxide nanoplatelets are provided, having anaverage platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the fifth aspect, the magnesium oxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the fifth aspect, the magnesium oxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the fifth aspect, the magnesium oxide nanoplateletsfurther comprise an additional metal oxide selected from the groupconsisting of SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃,NiO, Ni₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂, andmixtures thereof.

In a sixth aspect, a method of producing magnesium hydroxidenanoplatelets is provided, the method comprising the steps of providingan electrolyzer comprising an anode compartment, a cathode compartment,and a center compartment situated between the anode compartment and thecathode compartment, and separated from the anode compartment and thecathode compartment by ion selective membranes; adding a solution ofelectrolyte at a pH of about 8 to the anode compartment; adding asolution of up to about 50 wt. % sodium hydroxide at a pH of 8 or higherto the cathode compartment; adding a solution of a second electrolyte tothe center compartment, wherein the solution has from about 30,000 ppmchloride ion to about 200,000 ppm chloride ion; operating the cathodecompartment at an amperage of 3.75 amps per square inch or less, wherebyhydroxide ion is generated in the cathode compartment and migratesthrough its ion selective membrane into the center compartment, andwhereby sodium ion is generated in the anode compartment and migratesthrough its ion selective membrane into the center compartment; andthereafter adding to the center compartment a solution of solublemagnesium ion and a third electrolyte, the solution having from about300 ppm to 100,000 ppm magnesium ions and from about 5000 ppm to about200,000 ppm anions, whereby the soluble magnesium ion reacts withhydroxide ion to yield magnesium hydroxide nanoplatelets, wherein aresidence time in the center compartment of the magnesium hydroxidenanoplatelets is from about 0.1 minutes to about 10 minutes.

In an embodiment of the sixth aspect, an additional soluble metal ion isadded to the center compartment, wherein the additional soluble metalion is selected from the group consisting of strontium ion, barium ion,calcium ion, titanium ion, zirconium ion, iron ion, vanadium ion,manganese ion, nickel ion, copper ion, aluminum ion, cobalt ion, siliconion, zinc ion, silver ion, cerium ion, and mixtures thereof.

In an embodiment of the sixth aspect, the solution comprises water.

In an embodiment of the sixth aspect, the solution of soluble magnesiumion and an electrolyte is adjusted to a pH of 4.5 or less, wherebycarbonates are removed from the solution.

In an embodiment of the sixth aspect, the solution of soluble magnesiumion and an electrolyte is added to the center compartment at atemperature of from about 60° F. to about 190° F.

In an embodiment of the sixth aspect, the method further comprises thestep of removing residual water from the magnesium hydroxidenanoplatelets, whereby dried magnesium hydroxide nanoplatelets areobtained.

In an embodiment of the sixth aspect, the method further comprises thestep of applying heat to one side of the dried magnesium hydroxidenanoplatelets, whereby magnesium hydroxide is converted to magnesiumoxide through a portion of a thickness of the nanoplatelets, causingthem to roll into nanotubes, whereby magnesium (hydr)oxide nanotubes areobtained.

In an embodiment of the sixth aspect, the method further comprises thestep of applying heat to the dried magnesium hydroxide nanoplatelets,whereby magnesium hydroxide is converted to magnesium oxide through thethickness of the nanoplatelets, whereby magnesium oxide nanoplateletsare obtained.

In an embodiment of the sixth aspect, the magnesium hydroxidenanoplatelets have an average platelet diameter of from about 30 nm toabout 3500 nm and an average thickness of from about 1 nm to about 400nm.

In an embodiment of the sixth aspect, the magnesium hydroxidenanoplatelets have an average platelet diameter of from about 40 nm toabout 120 nm and an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the sixth aspect, the first, second, and thirdelectrolyte is sodium chloride.

In a seventh aspect, nickel hydroxide nanoplatelets are provided, havingan average platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets have an average platelet diameter of from about 40 nm toabout 120 nm and an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets have an average aspect ratio of from about 15 to about 70,an average BET specific surface area of from about 100 m²/g to about 150m²/g, and an average zeta potential of from about +60 mV to about −60mV.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets have an average aspect ratio of from about 15 to about 70,an average BET specific surface area of from about 100 m²/g to about 150m²/g, and an average zeta potential of from about −4 mV to about −5 mV.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets further comprise a second metal hydroxide selected fromthe group consisting of Mg(OH)₂, Ca(OH)₂, Al(OH)₃, Sr(OH)₂, Ba(OH)₂,Fe(OH)₃, Cu(OH)₂, Co(OH)₂, Zn(OH)₂, AgOH, and mixtures thereof.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets further comprise at least one metal oxide. In someembodiments, the metal oxide is selected from the group consisting ofMgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, CuO,Ni₂O₃, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂], and mixturesthereof.

In an embodiment of the seventh aspect, the nickel hydroxidenanoplatelets are in a form of rolled nanotubes.

In an eighth aspect, nickel oxide nanoplatelets are provided, having anaverage platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the eighth aspect, the nickel oxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the eighth aspect, the nickel oxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the eighth aspect, the nickel oxide nanoplateletsfurther comprise an additional metal oxide selected from the groupconsisting of MgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃,Fe₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂, andmixtures thereof.

In a ninth aspect, a method of producing nickel hydroxide nanoplateletsis provided, the method comprising the steps of providing anelectrolyzer comprising an anode compartment, a cathode compartment, anda center compartment situated between the anode compartment and thecathode compartment, and separated from the anode compartment and thecathode compartment by ion selective membranes; adding a solution ofelectrolyte at a pH of about 8 to the anode compartment; adding asolution of up to about 50 wt. % sodium hydroxide at a pH of 8 or higherto the cathode compartment; adding a solution of a second electrolyte tothe center compartment, wherein the solution has from about 30,000 ppmchloride ion to about 200,000 ppm chloride ion; operating the cathodecompartment at an amperage of 3.75 amps per square inch or less, wherebyhydroxide ion is generated in the cathode compartment and migratesthrough its ion selective membrane into the center compartment, andwhereby sodium ion is generated in the anode compartment and migratesthrough its ion selective membrane into the center compartment; andthereafter adding to the center compartment a solution of soluble nickelion and a third electrolyte, the solution having from about 300 ppm to100,000 ppm nickel ions and from about 5000 ppm to about 200,000 ppmanions, whereby the soluble nickel ion reacts with hydroxide ion toyield nickel hydroxide nanoplatelets, wherein a residence time in thecenter compartment of the nickel hydroxide nanoplatelets is from about0.1 minutes to about 10 minutes.

In an embodiment of the ninth aspect, an additional soluble metal ion isadded to the center compartment, wherein the additional soluble metalion is selected from the group consisting of magnesium ion, strontiumion, barium ion, calcium ion, titanium ion, zirconium ion, iron ion,vanadium ion, manganese ion, copper ion, aluminum ion, cobalt ion,silicon ion, zinc ion, silver ion, cerium ion, and mixtures thereof.

In an embodiment of the ninth aspect, the solution comprises water.

In an embodiment of the ninth aspect, the solution of soluble nickel ionand an electrolyte is adjusted to a pH of 4.5 or less, wherebycarbonates are removed from the solution.

In an embodiment of the ninth aspect, the solution of soluble nickel ionand an electrolyte is added to the center compartment at a temperatureof from about 60° F. to about 190° F.

In an embodiment of the ninth aspect, the method further comprises thestep of removing residual water from the nickel hydroxide nanoplatelets,whereby dried nickel hydroxide nanoplatelets are obtained.

In an embodiment of the ninth aspect, the method further comprises thestep of applying heat to one side of the dried nickel hydroxidenanoplatelets, whereby nickel hydroxide is converted to nickel oxidethrough a portion of a thickness of the nanoplatelets, causing them toroll into nanotubes, whereby nickel (hydr)oxide nanotubes are obtained.

In an embodiment of the ninth aspect, the method further comprises thestep of applying heat to the dried nickel hydroxide nanoplatelets,whereby nickel hydroxide is converted to nickel oxide through thethickness of the nanoplatelets, whereby nickel oxide nanoplatelets areobtained.

In an embodiment of the ninth aspect, the nickel hydroxide nanoplateletshave an average platelet diameter of from about 30 nm to about 3500 nmand an average thickness of from about 1 nm to about 400 nm.

In an embodiment of the ninth aspect, the nickel hydroxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the ninth aspect, the first electrolyte, secondelectrolyte, and third electrolyte is sodium chloride.

In a tenth aspect, copper hydroxide nanoplatelets are provided, havingan average platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about −4 mV to about −5 mV.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletsfurther comprise a second metal hydroxide selected from the groupconsisting of Mg(OH)₂, Ca(OH)₂, Al(OH)₃, Sr(OH)₂, Ba(OH)₂, Fe(OH)₃,Ni(OH)₂, Co(OH)₂, Zn(OH)₂, AgOH, and mixtures thereof.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletsfurther comprise at least one metal oxide. In some embodiments, themetal oxide is selected from the group consisting of MgO, SrO, BaO, CaO,TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, Ni₂O₃, Al₂O₃, SiO₂, ZnO,Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂], and mixtures thereof.

In an embodiment of the tenth aspect, the copper hydroxide nanoplateletsare in a form of rolled nanotubes.

In an eleventh aspect, copper oxide nanoplatelets are provided, havingan average platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.

In an embodiment of the eleventh aspect, the copper oxide nanoplateletshave an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the eleventh aspect, the copper oxide nanoplateletshave an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV.

In an embodiment of the eleventh aspect, the copper oxide nanoplateletsfurther comprise an additional metal oxide selected from the groupconsisting of MgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃,Fe₂O₃, NiO, CuO, Ni₂O₃, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂,and mixtures thereof.

In a twelfth aspect, a method of producing copper hydroxidenanoplatelets is provided, the method comprising the steps of providingan electrolyzer comprising an anode compartment, a cathode compartment,and a center compartment situated between the anode compartment and thecathode compartment, and separated from the anode compartment and thecathode compartment by ion selective membranes; adding a solution ofelectrolyte at a pH of about 8 to the anode compartment; adding asolution of up to about 50 wt. % sodium hydroxide at a pH of 8 or higherto the cathode compartment; adding a solution of a second electrolyte tothe center compartment, wherein the solution has from about 30,000 ppmchloride ion to about 200,000 ppm chloride ion; operating the cathodecompartment at an amperage of 3.75 amps per square inch or less, wherebyhydroxide ion is generated in the cathode compartment and migratesthrough its ion selective membrane into the center compartment, andwhereby sodium ion is generated in the anode compartment and migratesthrough its ion selective membrane into the center compartment; andthereafter adding to the center compartment a solution of soluble copperion and a third electrolyte, the solution having from about 300 ppm to100,000 ppm copper ions and from about 5000 ppm to about 200,000 ppmanions, whereby the soluble copper ion reacts with hydroxide ion toyield copper hydroxide nanoplatelets, wherein a residence time in thecenter compartment of the copper hydroxide nanoplatelets is from about0.1 minutes to about 10 minutes.

In an embodiment of the twelfth aspect, an additional soluble metal ionis added to the center compartment, wherein the additional soluble metalion is selected from the group consisting of magnesium ion, strontiumion, barium ion, calcium ion, titanium ion, zirconium ion, iron ion,vanadium ion, manganese ion, nickel ion, aluminum ion, cobalt ion,silicon ion, zinc ion, silver ion, cerium ion, and mixtures thereof.

In an embodiment of the twelfth aspect, the solution comprises water.

In an embodiment of the twelfth aspect, the solution of soluble copperion and an electrolyte is adjusted to a pH of 4.5 or less, wherebycarbonates are removed from the solution.

In an embodiment of the twelfth aspect, the solution of soluble copperion and an electrolyte is added to the center compartment at atemperature of from about 60OF to about 190° F.

In an embodiment of the twelfth aspect, the method further comprises thestep of removing residual water from the copper hydroxide nanoplatelets,whereby dried copper hydroxide nanoplatelets are obtained.

In an embodiment of the twelfth aspect, the method further comprises thestep of applying heat to one side of the dried copper hydroxidenanoplatelets, whereby copper hydroxide is converted to copper oxidethrough a portion of a thickness of the nanoplatelets, causing them toroll into nanotubes, whereby copper (hydr)oxide nanotubes are obtained.

In an embodiment of the twelfth aspect, the method further comprises thestep of applying heat to the dried copper hydroxide nanoplatelets,whereby copper hydroxide is converted to copper oxide through thethickness of the nanoplatelets, whereby copper oxide nanoplatelets areobtained.

In an embodiment of the twelfth aspect, the copper hydroxidenanoplatelets have an average platelet diameter of from about 30 nm toabout 3500 nm and an average thickness of from about 1 nm to about 400nm.

In an embodiment of the twelfth aspect, the copper hydroxidenanoplatelets have an average platelet diameter of from about 40 nm toabout 120 nm and an average thickness of from about 1 nm to about 4 nm.

In an embodiment of the twelfth aspect, the first electrolyte, secondelectrolyte, and third electrolyte is sodium chloride.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is an energy dispersive x-ray spectrum obtained from Mg(OH)₂nanoparticles within a slurry.

FIG. 2 is a diffraction pattern obtained for Mg(OH)₂ slurry particles.

FIG. 3 is a scanning transmission electron micrograph image of Mg(OH)₂slurry particles.

FIG. 4 is a transmission electron micrograph of Mg(OH)₂ slurryparticles.

FIG. 5 is an atomic force micrograph of a Mg(OH)₂ dispersion.

FIG. 6 is a BET surface area plot of Mg(OH)₂ nanoparticles within aslurry.

FIGS. 7-10 are electron micrographs of Mg(OH)₂ nanoparticles fromslurry.

FIG. 11 is an EDS spectrum of Mg(OH)₂ nanoparticles from slurry.

FIGS. 12A-H, 13A-C, and 14A-C are electron micrographs of Mg(OH)₂nanoparticle samples from slurry.

FIG. 15 depicts the dispersive X-ray spectrum obtained from nickelhydroxide nanoparticles doped with magnesium within a slurry.

FIGS. 16A-C depict micrograph images of nickel hydroxide nanoparticlesdoped with magnesium.

FIG. 17 depicts the dispersive X-ray spectrum obtained from copperhydroxide nanoparticles within a slurry.

FIG. 18A-B depict micrograph images of copper hydroxide nanoparticles.

FIG. 19 is a schematic depiction a process of decontaminating chemicaland biological agents using magnesium hydroxide.

FIG. 20 depicts surface morphology of magnesium hydroxide nanoplatelets.

FIG. 21 is a schematic depiction of pressure-assisted orientation ofMg(OH)₂ nanoplatelets.

FIG. 22 is a schematic depiction of formation of self-assembledpositively and negatively charged thin layers.

FIG. 23 is a schematic depiction of a layer-by-layer approach topreparing a nacre mimicked nanocomposite.

FIG. 24 is a schematic depiction of a shear thickening mechanism for thebody armor materials.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

Methods and methodologies used to produce nanoplatelets and other formsof metal hydroxides are provided. The base materials used to make theprocess feedstock include, for example, a metal chloride (e.g.,magnesium chloride (MgCl₂)) and sodium chloride (NaCl). Suitable basematerials include commercially available bulk forms of sodium chlorideand metal chlorides. A suitable form of magnesium chloride is marketedas FreezGard® magnesium chloride available from North American SaltCompany of Overland Park, Kans. While magnesium chloride is particularlypreferred, other sources of soluble magnesium ion can also be employed,for example other magnesium halides such as magnesium bromide andmagnesium iodide, magnesium nitrate, and magnesium sulfide. Likewise,other metal ions (in the form of metal chlorides or other soluble metalions), including, but not limited to, beryllium (Be), magnesium (Mg),calcium (Ca), strontium (Sr), barium (Ba), radium (Ra), scandium (Sc),titanium (Ti), vanadium (V), chromium (Cr), manganese (Mn), iron (Fe),cobalt (Co), nickel (Ni), copper (Cu), zinc (Zn), yttrium (Y), zirconium(Zr), niobium (Nb), molybdenum (Mo), technetium (Tc), ruthenium (Ru),rhodium (Rh), palladium (Pd), silver (Ag), cadmium (Cd), lutetium (Lu),hafnium (Hf), tantalum (Ta), tungsten (W), rhenium (Re), osmium (Os),iridium (Ir), platinum (Pt), silver (Au), mercury (Hg), lawrencium (Lr),rutherfordium (Rf), dubnium (Db), seaborgium (Sg), bohrium (Bh), hassium(Hs), meitnerium (Mt), darmstadtium (Ds), roentgenium (Rg), unubium(Uub), aluminum (Al), gallium (Ga), indium (In), tin (Sn), thallium(Tl), lead (Pb), and bismuth (Bi) can be employed to producenanoplatelets, nanotubes, and/or other particulate forms of variousmetal oxides and metal hydroxides. Metal oxides and hydroxides that canbe prepared according to the preferred embodiments include, but are notlimited to, MgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃,Fe₂O₃, NiO, Ni₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂,Mg(OH)₂, Ca(OH)₂, Al(OH)₃, Sr(OH)₂, Ba(OH)₂, Fe(OH)₃, Cu(OH)₃, Ni(OH)₂,Co(OH)₂, Zn(OH)₂, AgOH, mixed oxides and hydroxides of the foregoingmetals, mixed metal oxides and/or hydroxides, and other combinationsthereof.

The sodium chloride brings the electrolyte content of the water up so asto reduce its electrical resistance, thereby reducing electrical costsfor the production of the metal hydroxide nanoplatelets or other metaloxide or hydroxide forms. While it is generally preferred to employsodium chloride, other suitable electrolytes can also be employed, aloneor in combination. Common electrolytes include ions such as sodium(Na⁺), lithium (Li⁺), potassium (K⁺), calcium (Ca²⁺), magnesium (Mg²⁺),chloride (Cl⁻), fluoride (F⁻), bromide (Br⁻), and the like.

The metal chloride and sodium chloride are mixed in a feedstock tank,with reverse osmosis (RO) water as a solvent to yield an ionic andgelatinous fluid. RO water is typically prepared by taking regular tapwater, running it through a water softener, and then running thesoftened water through a reverse osmosis system. The purity of the ROwater is similar to that of de-ionized (DI) water, but is considerablycheaper to produce. While RO water is generally preferred as a solventdue to its reduced costs, DI water, or water of similar purity can beemployed as well. In certain embodiments, water of lesser purity (e.g.,tap water) can be employed in the preparation of the metal (hydr)oxidesof preferred embodiments.

The quantity of metal chloride and sodium chloride dissolved in thewater is selected, along with other process conditions, so as to yieldmetal hydroxide particles of desired properties (e.g., particle sizeand/or morphology). In preferred embodiments, metal chloride is added tothe RO water so as to yield a brine containing from about 300 ppm (orless) to about 100,000 ppm (or more) of metal ions, preferably about1,500 ppm of metal ions. Sodium chloride is added to the RO water so asto yield a brine containing from about 5,000 ppm to about 200,000 ppmCl⁻, preferably about 43,000 ppm Cl⁻.

About 8 fluid ounces (237 mg) of concentrated muriatic acid(hydrochloric acid) is added to 400 gallons (1,514 liters) of RO waterthat has been blended with metal chloride and sodium chloride to achievea pH of approximately 4.5. At that pH level, any carbonates that arepresent in the salts are dissolved into the water. While a pH of 4.5 isparticularly preferred, any suitable pH that will dissolve carbonate canalso be employed. The dissolved carbonates are then removed byconversion into CO₂ gas which is degassed from the system, therebyminimizing carbonates solids forming in the precipitation operation.While muriatic acid is preferred for use in adjusting pH, other suitableacids can also be employed (e.g., hydrobromic acid, sulfuric acid, andthe like). Depending upon the carbonate content (or lack thereof) of thefeedstock materials, it can not be necessary to adjust the pH.Alternatively, in certain embodiments, the presence of carbonates solidsin the precipitation operation is tolerable, and thus no specialprocedures for removing them are performed.

After the system is degassed of carbon dioxide (CO₂), the metalion-containing feedstock is circulated through a heating system. It ispreferred to operate the system at a temperature of from about 40° F. toabout 200° F. (about 4° C. to about 93° C.), preferably from about 50°F. to about 190° F. (about 10° C. to about 88° C.), more preferably fromabout 60° F. to about 160° F. (about 16° C. to about 71° C.), even morepreferably about 110° F. (about 43° C.). In some embodiments, the systemcan be operated at any suitable temperature from about the freezingpoint of the feedstock to about the boiling point of the feedstock. Thefeedstock is then sent to an electrolyzer divided into threecompartments: an anode compartment; a cathode compartment; and a centerfluid separator compartment between the anode and cathode compartmentsthat separates fluids of the anodic compartment from the fluids of thecathodic compartment. While this particular electrolyzer configurationis generally preferred, other suitable configurations can also beemployed. Other suitable electrolyzer configurations are employed inU.S. Pat. Nos. 7,048,843, 6,235,185, 6,375,825, 5,660,709, 5,496,454,5,785,833, the disclosures of which are herein incorporated by referencein their entirety. Still other suitable electrolyzer configurations areoutlined in U.S. Patent Publication Nos. 2003/0082095, 2004/0197255,2007/0113779, and 2004/0108220, the disclosures of which are hereinincorporated by reference in their entirety. The methods disclosed inthese references can differ from those of the preferred embodiments, forexample, with respect to parameters and the location of reaction. Thesedifferences result in nanoparticles that differ in size and morphologyfrom the nanoplatelets produced according to the methods of preferredembodiments. Within the anode compartment is an anode electrode that isconstructed out of titanium and coated with iridium oxide, and is in theform of a mesh with ¼-inch holes throughout (manufactured by UhdenoraS.p.A. of Milan, Italy; UHDE BM-2.7, anode compartment half shellincluding the anode electrode). While such electrodes are generallypreferred, other electrodes and electrode configurations can also beemployed (e.g., other metals such as platinum group metals (platinum orruthenium, or oxides thereof), or plate or bar shaped electrodes insteadof mesh). The compartment can operate from 0.1 to 3.75 amps per squareinch. However, in certain embodiments it can be acceptable or evendesirable to operate at lower or higher amperages. The electricalcircuit for the anode compartment chamber can operate or be operated ineither a series or parallel configuration, as is commonly employed inthe chlor-alkali industry. NaCl in the anode compartment is split intochlorine gas and sodium ion (Na⁺). The sodium ion travels through an ionselective membrane (manufactured by The Dow Chemical Company of Midland,Mich.) into the center compartment. Any suitable membrane can beemployed that is permeable to sodium ions but resists the flow of waterthere through. Examples of ion selective membranes include glassmembranes (e.g., silicates of chalcogenides), crystalline membranes(e.g., fluoride selective electrodes based on LaF₃ crystals), and ionexchange resin membranes (anion exchange, cation exchange, and mixed ionexchange membranes such as those prepared from polyvinyl, polystyrene,polyethylene, polyesters, epoxies, and silicones).

The cathode electrode, which is in the cathode chamber, is preferablyconstructed out of a nickel alloy in a perforated form to create manyflux lines there through (manufactured by Uhdenora S.p.A. of Milan,Italy; UHDE BM-2.7, cathode half shell including electrode).Alternatively, the cathode electrode can be constructed of #316stainless steel. While these electrode configurations and materials areparticularly preferred, other electrode configurations and materials canalso be suitable for use (e.g., electrode materials and configurationsas described above with reference to the anode electrode), with processconditions adjusted accordingly. The cathode compartment preferablyoperates with a sodium hydroxide solution up to about 50% by weight orcan operate with a NaCl solution or other electrolyte solution. Thecathode compartment can also operate at 3.75 amps per square inch orless. The electrical circuit for the cathode compartment chamber canoperate or be operated in either a series or parallel configuration.Water is split in the cathode chamber to yield hydrogen gas and hydroxylions. An ion selective membrane rests on the cathode electrode and facesthe center fluid separator compartment, allowing hydroxyl ions to passthere through.

The fluid within the anodic compartment is preferably at a pH of about1, and the fluid within the cathode compartment is preferably at a pHabove 8.5. Electricity can flow freely through the center fluidseparator compartment, but hydrophobic ion selective membranes restrictthe movement of water into it, thereby allowing the cathode compartmentand anode compartment to contain their own separate fluids. The centercompartment includes an inlet and an outlet and is situated between thetwo ion selective membranes (manufactured by The Dow Chemical Company ofMidland, Mich.). The center chamber operates with a positive pressure tokeep each of the membranes in place. Suitable membranes includeelectrodeionization membranes such as those sold under the trademarkOMEXELL™ by The Dow Chemical Company.

The ion selective membranes selectively allow ions to pass into thecenter fluid separator compartment where metal hydroxide precipitationtakes place, and from which metal hydroxide nanoplatelets are harvested.This process occurs as follows. A sodium ion passes through the anodeion selective membrane into the center compartment, and a hydroxyl ionpasses through the cathode ion selective membrane into the centercompartment. Metal ions from the metal chloride in the centercompartment react with hydroxyl ions to form solid metal hydroxideleaving a free chlorine ion. The sodium ion from the anode compartmentreacts with the free chlorine ion from the metal chloride in the centercompartment to form sodium chloride.

Prior to initiating metal hydroxide precipitation in the electrolyzer,RO water is heated in a tank to a temperature of about 120° F. Sodiumchloride is added to the RO water until a Cl⁻ concentration of about30,000 parts per million to about 200,000 parts per million is reached,yielding a very conductive solution. In a preferred embodiment, sodiumchloride is added to the RO water until a Cl⁻ concentration of about75,000 parts per million is reached. The RO water with added sodiumchloride at the elevated temperature is pumped into the center chamberto fill it completely. The cathode and anode compartments are thenfilled with their respective fluids. Next, the current in theelectrolyzer is brought up to the desired level, preferably levels asdescribed above. Current in the electrolyzer can be brought to a currentof from about 4.00 Amps per square inch to about 0.10 Amps per squareinch. In certain embodiment, it may be desirable to achieve a currenthigher than 4.00 Amps per square inch or lower than 0.10 Amps per squareinch. In a preferred embodiment, the current is brought to about 0.75Amps per square inch. The current generates hydroxyl (OH ions in thecathode chamber by splitting water, thereby driving the pH up.

When a desired pH, such as a pH of about 11, is reached throughout thefluid, the metal-containing feedstock is added to the center fluidseparator compartment. When the metal-containing feedstock is added tothe high pH RO water with added sodium chloride, the metal ions areattracted to the electrode flux grid line, where they react withhydroxyls to yield metal hydroxide. After nucleation, metal hydroxideadds to the nucleus in a flat plane along the flux lines, such that inthe remaining crystal growth, metal hydroxides attach around the borderof the nucleation crystal in conformity with the flux lines, yieldingcrystalline nanoplatelets in the center compartment. By adjustingselected variables, the particle size and morphology of the metalhydroxide can be controlled. The residence time of feedstock flowthrough the center compartment can be adjusted to set the particle size(with faster flow rates resulting in smaller particle size). Feedstockresidence times of from about 0.1 minute or less to about 10 minutes ormore are generally preferred. The quality of flux line by the energypassing between the opposing compartments and temperature can beadjusted to control the speed of the reaction. By adjusting theseparameters, metal hydroxide platelets of uniform size can be produced.Tight size distributions can be obtained for particles having an averageplatelet size of 3.5 microns in the X/Y dimension and 100 nm in the Zdimension down to particles having an average platelet size of 30 nm inthe X/Y dimension and 2.5 nm in the Z dimension. Generally, the fasterthe nanoplatelets are harvested, as long as a pH above the precipitationpoint is maintained for the metal being produced, the smaller theresulting nanoplatelets. The preferred dimensions will depend upon theapplication and the system will be adjusted accordingly.

Sodium chloride (NaCl) is converted to chlorine (Cl₂ gas) in the anodecompartment, and the resulting sodium ion migrates to the cathodecompartment. As discussed above, in the cathode compartment water issplit to release hydrogen gas (H₂ gas), leaving a hydroxyl ion whichcombines with a metal ion from the metal chloride to form metalhydroxide. Chloride ion combines with the sodium ion in the cathodecompartment to form sodium chloride.

The electrolyzer incorporates a pipe that allows elemental hydrogen gasgenerated during water splitting to leave the cathode compartment.Another pipe in the anode compartment allows elemental chlorine gasproduced to leave. In the production of magnesium hydroxide,approximately 6.34 cubic feet of hydrogen gas weighing 0.07 pounds isgenerated for every pound of magnesium hydroxide that is produced, andapproximately 6 cubic feet of chlorine gas weighing 1.2 pounds isgenerated for every pound of magnesium hydroxide produced. The hydrogenand/or chlorine gas can be disposed of, or captured for use asfeedstocks in other processes. In preferred embodiments, the chlorinegas can be employed to produce sodium hydrochloric bleach at a 15%density. While a pipe is a particularly preferred component for ventinggas, other components can also be employed (e.g., a passageway, a gaspermeable sheet, or the like).

The nanoplatelet-containing fluid is removed to a catch basin, and thento a centrifuge where metal hydroxide is separated from the supernatantcontaining ions in water. The supernatant is recycled back into thefeedstock system so as to recover metal ions, sodium ions, and chlorineions. After the centrifuge discharges the metal hydroxide solids in theform of a gel, the solids are washed. Preferably, approximately 5gallons of gel, corresponding to about 5 pounds of metal hydroxidedry-weight, are washed with approximately 50 gallons of water. Thewashed metal hydroxide is cycled back through the centrifuge and therecovered gel is washed again. Preferably, four washes are conducted toyield metal hydroxide of approximately 99+% purity. Table 1 presentspurity data for three magnesium hydroxide nanoplatelet samples subjectedto the preferred washing cycle. The first wash is 10:1 (e.g., 5 gallonsgel to 50 gallons water), the second wash is 100:1, the third wash is1,000:1, and the fourth wash is 10,000:1 in the specified dilutionratios. Depending upon the desired purity of the resulting metalhydroxide nanoplatelets, fewer (e.g., only one, two or three washes)steps can be conducted, or additional (e.g., five or more washes, orother separation processes) steps can be conducted. TABLE 1A Purity Datafor Magnesium Hydroxide Sample 1 Sample 1 Result Detection Test (Wt. %)Limit Method Calcium 0.0078 0.0001 ICP Chloride, Total 0.1298 0.0001SOP-CL Iron 0.0612 0.0001 ICP Magnesium Hydroxide 99.46 0.0001 ICPMoisture 92.91 0.0001 OVEN Silica (SiO₂) 0.192 0.0001 ICP Sodium 0.0140.0001 ICP Sulfate (SO₄) <0.0001 0.0001 375.4

TABLE 1B Purity Data for Magnesium Hydroxide Sample 2 Sample 2 ResultDetection Test (Wt. %) Limit Method Calcium 0.286 0.0001 ICP Chloride,Total 0.1706 0.0001 SOP-CL Iron 0.0451 0.0001 ICP Magnesium Hydroxide99.02 0.0001 ICP Moisture 36.05 0.0001 OVEN Silica (SiO₂) 0.162 0.0001ICP Sodium 0.0084 0.0001 ICP Sulfate (SO₄) <0.0001 0.0001 375.4

TABLE 1C Purity Data for Magnesium Hydroxide Sample 3 Sample 3 ResultDetection Test (Wt. %) Limit Method Calcium 0.0099 0.0001 ICP Chloride,Total 0.1136 0.0001 SOP-CL Iron 0.0673 0.0001 ICP Magnesium Hydroxide99.46 0.0001 ICP Moisture 2.72 0.0001 OVEN Silica (SiO₂) 0.178 0.0001ICP Sodium 0.0329 0.0001 ICP Sulfate (SO₄) <0.0001 0.0001 375.4

Depending upon the end use, the washed metal hydroxide nanoplatelets canbe used in gel form (the product from the centrifuge), or can be subjectto drying. In preferred embodiments, the metal hydroxide can be driedusing spray drying equipment using a rotary atomizer or other nozzleconfiguration. Nozzle inlet temperatures of 280° C. and outlettemperatures of 120° C. for spray drying metal hydroxide can beemployed; however, any suitable temperature or method for removingliquid from the metal hydroxide can be employed.

When the magnesium hydroxide particles in gel form are subjected todrying in a dryer, a particle form referred to as the “Desert Roseconfiguration” can be obtained. Magnesium hydroxide in the Desert Roseconfiguration is particularly well suited for use in the polymer andcoatings industry.

Under the torque of compounding, the lightly-bound together petals ofthe Desert Rose disassemble to separate nanoplatelets, which areparticularly useful, for example as a flame retardant. Alternatively,magnesium hydroxide in the gel state or slurry form can be used in thepaper industry.

Magnesium Hydroxide nanoplatelets in slurry form were prepared by themethod described above. Particularly, the center compartment of theelectrolyzer was filled with RO water containing NaCl at a concentrationof 75,000 ppm. The cathode and anode compartments were subsequentlyfilled with RO water containing NaCl at a concentration of 75,000 ppm.The pressure in the center compartment was maintained at a higher levelthan that of the anode and cathode compartments to keep the selectiveion membrane in place. The current in the machine was brought up to 7volts at 0.75 Amps/Square Inch. The temperature of the contents withinthe three compartments was maintained at about 110° F. (about 43° C.) ata pH of about 11. Feedstock was formulated with a final concentration ofCl⁻ ions at 30,000 ppm and Mg²⁺ ions at 1500 ppm. The feedstock was fedthrough the center compartment at a rate of one gallon per minute,resulting in a residence time of 10 minutes. Material was collected inthe catch basin and centrifuged. Slurry collected after centrifugationwas tested to determine the characteristics of the particles within theslurry. The chemical composition of the slurry was determined by energydispersive x-ray spectrometric analysis of a dried sample in a JEOL JSM6500 field emission scanning electron microscope using a Noran Vantageenergy dispersive x-ray spectrometer. transmission electron micrographswere obtained using either a Philips 420 or a Philips CM120 transmissionelectron microscope equipped with an SIA digital imaging system. Sampleswere also examined by atomic force microscopy (AFM). BET specificsurface areas of the samples as well as the zeta potential were alsocalculated. A summary of the results of the characterization is given inTable 2. TABLE 2 Summary of Characterization Efforts Crystal Structure:Brucite: Mg(OH)2 Platelet Diameter: (FESEM) 72 +/− 21 nm (TEM) 72 +/− 28nm (AFM) 80.9 +/− 29.5 nm Platelet Thickness: (FESEM) not available(TEM) 2.5 +/− 0.8 nm (AFM) 2.3 +/− 1.1 nm Aspect Ratio: (FESEM) notavailable (TEM) 30 +/− 17 (AFM) 43 +/− 25 Equivalent Spherical Diameter:(FESEM) not available (TEM) 26 +/− 8 nm (AFM) 27 +/− 7 nm BET SpecificSurface Area: 129 m²/g Zeta Potential: −4.2 mV

FIG. 1 is an energy dispersive x-ray spectrum obtained from particles ofthe slurry The spectrum confirmed that the particles were composed ofmagnesium and oxygen, which is consistent with Mg(OH)₂, as the method isnot sensitive to hydrogen. The Energy-Dispersive X-ray Spectroscopy(EDS) spectrum was consistent with that expected for magnesiumhydroxide. X-ray Diffraction analysis indicated the particles had acrystal structure characterized as brucite (Mg(OH)₂). Table 3 shows theposition of the peaks in the pattern compared to known peaks forbrucite. FIG. 2 is the diffraction pattern obtained for the bruciteparticles. The relatively broad peaks in FIG. 2 are due to the verysmall particle size of the slurry particles. TABLE 3 X-ray DiffractionResults (CuKa, 40 kV, 20 mA, 0.05° steps, 4 sec. count time) Observed2-theta d-spacing d-spacing (Brucite) 19.00 4.67 å 4.77 å 33.15 2.702.72 38.20 2.36 2.37 50.85 1.80 1.79 58.95 1.57 1.57 62.30 1.49 1.49

To determine particle size and morphology, particles in the slurry weredispersed in isopropanol, ultrasonicated, and transferred to theanalytical substrate in an atomizing spray. Dispersed samples wereprepared on a thin carbon film supported by a standard copper TEM grid.For Field Emission Scanning Electron Microscopy (FESEM) examination, theTEM grid bearing dispersed particles was placed in a JEOL scanningtransmission electron microscopy (STEM) sample holder and the sampleholder placed in the FESEM. FIG. 3 shows a typical STEM image ofdispersed particles.

STEM images of several fields of view were obtained using a NoranVantage digital imaging system, and the diameters of individualparticles were sized using the image processing and particle sizingfunctions of ImageJ, an image measurement software package distributedand maintained by the National Institutes of Health. The results ofmeasurement of the diameter of 156 platelets by FESEM are summarized inTable 4. TABLE 4 FESEM Particle Diameter Measurement Results ParticleMajor Axis Minor Average Number (nm) Axis (nm) Diameter (nm)  1 62 46 54 2 57 46 51  3 74 55 65  4 110 106 108  5 96 76 86  6 121 70 96  7 42 3639  8 68 57 63  9 61 49 55 10 97 70 83 11 68 54 61 12 77 70 74 13 74 6570 14 108 89 99 15 47 38 42 17 84 75 79 18 119 68 94 19 65 52 58 20 9377 85 21 81 64 72 22 94 84 89 23 40 26 33 24 35 29 32 25 65 57 61 26 138101 120 27 91 74 83 28 106 47 77 29 98 87 92 30 60 48 54 31 100 57 79 32101 75 88 33 47 29 38 34 83 41 62 35 107 97 102 36 109 83 96 37 101 7890 38 162 129 146 39 93 69 81 40 152 127 139 41 45 39 42 43 85 75 80 4456 54 55 45 100 85 93 46 115 95 105 47 69 67 68 48 118 108 113 49 61 5357 50 102 92 97 51 81 61 71 52 59 40 50 53 78 65 71 54 128 69 98 55 122109 115 57 97 73 85 58 56 35 45 59 68 49 58 60 45 39 42 61 85 60 73 6256 45 51 63 90 65 78 64 44 36 40 65 84 65 74 66 108 77 93 67 73 69 71 6887 41 64 69 93 68 81 70 87 69 78 71 90 61 76 72 111 86 98 73 107 83 9574 86 72 79 75 86 71 79 76 45 38 41 77 70 61 66 78 94 68 81 79 117 95106 80 62 46 54 81 108 80 94 83 59 56 58 84 51 48 50 85 66 49 57 86 7168 69 87 64 42 53 88 76 32 54 89 55 46 50 90 73 67 70 91 45 40 42 92 10086 93 93 71 56 64 94 70 55 62 95 102 54 78 96 56 41 48 97 106 59 83 9850 35 42 99 107 70 88 100  66 57 62 101  68 60 64 102  73 54 64 103  8481 82 104  76 62 69 105  98 53 76 106  51 38 44 107  43 42 43 108  81 3759 109  76 62 69 110  103 63 83 111  80 54 67 112  51 39 45 113  110 6889 114  79 62 70 115  68 51 59 116  125 98 112 117  65 63 64 118  67 5661 119  108 96 102 120  60 48 54 121  85 79 82 122  164 76 120 123  8760 73 124  56 37 47 125  83 67 75 126  86 77 82 127  59 44 52 128  75 5766 129  64 58 61 130  51 45 48 131  83 44 64 132  56 45 50 133  68 38 53134  100 68 84 135  50 34 42 136  107 58 83 137  84 62 73 138  92 78 85139  57 52 55 140  68 56 62 141  84 54 69 143  85 72 79 144  104 81 93145  137 85 111 146  59 36 47 147  51 48 50 148  57 38 48 149  63 41 52150  74 59 67 151  74 61 68 152  82 76 79 153  83 53 68 155  75 66 70156  58 42 50 157  83 70 77 158  102 72 87 159  90 69 80 160  109 84 97average st dev 71.8 21.1

Field Emission Scanning Electron Microscopy (FESEM) showed particles inthe form of thin platelets in a narrow size distribution (approximately50 to 100 nm in the longest dimension). Of the platelets measured: 3.3%of platelets were from about 30 nm to about 40 nm in diameter; 14.9% ofplatelets were from about 41 nm to about 50 nm in diameter; 13% ofplatelets were from about 51 nm to about 60 nm in diameter; 20.1% ofplatelets were from about 61 nm to about 70 nm in diameter; 16.2% ofplatelets were from about 71 nm to about 80 nm in diameter; 14.3%% ofplatelets were from about 81 nm to aobut 90 nm in diameter; 9.7% ofplatelets were from about 91 nm to about 100 nm in diameter; 3.3% ofplatelets were from about 101 nm to about 110 nm in diameter; 3.9% ofplatelets were from about 111 nm to about 120 nm in diameter; 0.7% ofplatelets were from about 131 nm to about 140 nm in diameter; 0.7% ofplatelets were from about 141 nm to about 150 nm in diameter. TheEnergy-Dispersive X-ray Spectroscopy (EDS) spectrum was consistent withthta xpected for magnesium hydroxide.

Particle dispersions were prepared in a similar manner for TEM analysis.Clusters of platelets were analyzed, with some platelets orientedperpendicular to the viewing axis, allowing measurement of plateletdiameter as well as platelet thickness (FIG. 4). Table 5 contains theresults of particle diameter, thickness, and aspect ratios as measuredby TEM. TABLE 5 Particle Diameters, Thicknesses, Aspect Ratios andEquivalent Spherical Diameters from TEM Images Diam. Thick. AspectParticle (nm) (nm) Ratio ESD (nm)  1 43.7 1.4 31.0 15.9  2 87.3 2.9 30.132.1  3 53.7 2.9 18.4 23.3  4 55.6 2.2 25.5 21.6  5 49.2 2.7 18.2 21.4 6 36.4 2.4 15.2 16.8  7 44.9 2.0 23.0 18.1  8 77.3 1.7 44.3 25.0  940.0 2.9 13.8 19.1 10 52.0 1.4 36.8 17.9 11 70.5 2.4 29.6 26.1 12 58.52.0 29.3 21.7 13 115.7 2.7 42.3 38.0 14 74.8 1.7 42.9 24.5 15 50.2 2.917.2 22.2 16 60.3 2.8 21.9 24.7 17 52.5 2.4 21.7 21.6 18 74.1 2.5 29.727.4 19 71.6 3.8 19.1 30.7 20 36.6 2.6 14.2 17.3 21 38.3 2.2 17.7 16.822 69.5 2.7 25.4 27.1 23 62.2 3.1 20.1 26.2 24 61.7 2.5 24.8 24.2 2551.6 2.3 22.6 20.9 26 108.9 2.5 44.1 35.3 27 51.3 2.2 23.7 20.5 28 42.61.6 26.3 16.4 29 111.5 3.0 37.3 38.2 30 59.8 2.0 30.6 21.9 31 29.9 2.313.1 14.5 32 58.7 3.5 17.0 26.2 33 50.6 3.1 16.4 22.8 34 78.4 2.2 35.827.2 35 121.3 2.7 44.9 39.1 36 55.3 3.4 16.5 24.9 37 143.1 3.4 41.8 47.238 56.9 1.6 35.1 19.9 39 50.5 2.2 23.3 20.2 40 45.7 1.2 37.8 15.6 41114.6 3.7 31.1 41.7 42 90.5 3.1 29.2 33.6 43 84.1 1.5 54.3 25.4 44 97.72.1 47.6 30.9 45 118.2 2.1 57.2 35.1 46 49.3 1.5 33.9 17.4 47 31.8 2.016.3 14.3 48 48.6 2.4 20.0 20.5 49 50.5 1.2 41.7 16.7 50 41.1 2.8 14.919.1 51 117.8 2.1 56.6 35.1 52 45.3 1.5 31.2 16.5 53 55.9 2.3 24.4 22.154 40.9 1.7 23.4 16.4 55 92.9 2.6 35.6 32.3 56 96.4 1.0 96.6 24.0 5743.9 2.9 15.1 20.3 58 73.0 1.5 47.2 23.1 59 79.2 3.4 23.2 31.8 61 115.13.1 37.2 39.5 62 45.1 4.6 9.8 24.1 63 101.7 2.8 36.0 35.2 64 77.5 2.432.0 27.9 65 77.1 1.7 44.2 25.0 66 100.5 2.0 50.4 31.2 67 60.1 1.9 31.021.9 68 38.2 2.9 13.1 18.5 69 113.5 2.4 46.9 36.0 70 75.3 1.5 51.8 23.171 75.9 3.4 22.4 30.8 72 65.8 3.4 19.2 28.1 73 47.5 1.7 27.2 18.1 74102.9 2.2 47.5 32.5 75 57.8 1.9 29.9 21.3 76 48.6 2.4 20.1 20.5 77 132.72.4 54.9 40.0 78 156.0 1.1 144.1 34.0 79 111.2 3.5 31.9 40.2 80 62.5 3.517.7 27.4 81 33.3 2.8 11.8 16.8 82 61.7 3.2 19.0 26.5 83 55.2 2.8 19.623.4 84 71.0 2.8 25.2 27.7 85 72.9 4.9 14.8 34.0 86 165.2 3.4 48.3 51.987 92.7 2.9 31.9 33.5 88 52.6 3.2 16.2 23.8 89 46.2 2.7 16.9 20.6 9092.6 2.8 32.8 33.1 91 89.3 2.9 30.3 32.8 92 71.7 3.4 21.2 29.7 93 66.41.4 48.5 20.8 94 106.8 2.6 41.0 35.5 95 91.0 1.7 52.1 27.9 96 84.7 3.425.0 33.2 97 110.6 3.4 32.3 39.7 98 94.4 3.4 27.6 35.8 99 68.1 1.4 49.821.2 100  61.7 2.4 25.5 24.0 101  105.5 2.8 37.4 36.1 102  75.8 4.4 17.433.5 103  58.9 2.6 22.6 23.8 104  36.4 1.5 23.8 14.5 105  46.3 3.1 15.121.4 106  65.4 2.4 27.0 24.9 107  67.1 2.6 25.8 26.0 108  42.8 1.5 28.016.1 109  39.7 2.8 14.1 18.8 110  57.6 2.9 19.9 24.4 111  89.4 3.1 29.233.2 112  115.2 4.6 25.1 45.0 113  51.4 2.2 23.8 20.5 114  39.4 2.0 19.716.7 115  53.6 2.5 21.7 22.0 116  93.7 3.4 27.7 35.5 Average 71.4 2.530.5 26.3 Std Dev 28.2 0.8 16.9 7.9*ESD = Equivalent Spherical Diameter

Transmission Electron Microscopy (TEM) showed particles in the form ofthin platelets in a narrow size distribution (with approximately 85% ofthe particles within 30 to 100 nm in the longest dimension). Of theplatelets measured,0.9% of platelets were from about 21 nm to about 30nm in diameter; 8.6% of platelets were from about 31 nm to about 40 nmin diameter; 15.5% of platelets were from about 41 nm to about 50 nm indiameter; 21.6% of platelets were from about 51 nm to about 60 nm indiameter; 9.5% of platelets were from about 61 nm to about 70 nm indiameter; 13.8% of platelets were from about 71 nm to about 80 nm indiameter; 4.3% of platelets were from about 81 nm to about 90 nm indiameter; 7.8% of platelets were from about 91 nm to about 100 nm indiameter; 5.2% of platelets were from about 101 nm to about 110 nm indiameter; 8.6% of platelets were from about 111 nm to about 120 nm indiameter; 0.9% of platelets were from about 131 nm to about 140 nm indiameter; 0.9% of platelets were from about 141 nm to about 150 nm indiameter; 0.9% of platelets were from about 151 nm to about 160 nm indiameter; and 0.9% of platelets were from about 161 nm to about 170 nmin diameter.

The TEM images also showed particles with a narrow distribution ofthicknesses (the particles were within 1 nm to 5 nm in thickness). Ofthe platelets measured: 12.9% of platelets were from about 1.1 nm toabout 1.5 nm in thickness; 13.8% of platelets were from about 1.6 nm toabout 2.0 nm in thickness; 24.1% of platelets were from about 2.1 nm toabout 2.5 nm in thickness; 25% of platelets were from about 2.6 nm toabout 3.0 nm in thickness; 19% of platelets were from about 3.1 nm toabout 3.5 nm in thickness; 1.7% of platelets were from about 3.6 nm toabout 4.0 nm in thickness; 0.9% of platelets were from about 4.1 nm toabout 4.5 nm in thickness; and 2.6% of platelets were from about 4.6 nmto about 5.0 nm in thickness.

Additionally, the TEM images showed particles with a narrow distributionof equivalent spherical diameters (ESDs) (with approximately 85% of theparticles with ESDs of about 15 nm to about 35 nm). Of the plateletsmeasured: 2.6% had an ESD from about 11 nm to about 15 nm; 19.8% had anESD from about 16 nm to about 20 nm; 33.6% had an ESD from about 21 nmto about 25 nm; 12.1% had an ESD from about 26 nm to about 30 nm; 18.1%had an ESD from about 31 nm to about 35 nm; 10.3% had an ESD from about36 nm to about 40 nm; 1.7% had an ESD from about 41 nm to about 45 nm;0.9% had an ESD from about 46 nm to about 50 nm; and 0.9% had an ESDfrom about 51 nm to about 55 nm.

Similar particle dispersions as prepared for FESEM and TEM were preparedon mica substrates for atomic force microscopy (AFM). FIG. 5 is an AFMimage of a typical dispersion. Average particle diameters, thicknesses,and aspect ratios calculated by AFM are presented in Table 6. TABLE 6Particle Diameters, Thicknesses, Aspect Ratios and Equivalent SphericalDiameters from Atomic Force Microscopy (AFM) Diam. Thick. Aspect ESDParticle (nm) (nm) Ratio (nm)  1 45.7 3.1 14.6 21.4  2 32.9 2.8 11.716.6  3 34.3 2.0 17..2 15.2  4 37.1 2.2 17.3 16.4  5 31.8 2.0 15.9 14.5 6 36.6 5.6 6.5 22.4  7 39.3 2.0 19.6 16.7  8 41.7 2.3 18.1 18.2  9 37.02.3 16.5 16.7 10 42.4 2.1 20.2 17.8 11 38.5 1.9 20.3 16.2 12 39.6 2.516.1 17.9 13 40.2 2.9 14.1 19.0 14 42.4 4.7 9.0 23.3 15 50.8 2.4 21.221.0 16 43.3 2.7 16.0 19.7 17 42.3 2.4 18.0 18.5 18 50.7 2.6 19.5 21.619 46.2 3.0 15.4 21.2 20 53.1 2.9 18.3 23.1 21 50.2 5.4 9.3 27.3 22 55.23.1 17.8 24.2 23 47.4 2.5 18.9 20.3 24 54.0 0.6 89.9 13.8 25 53.4 2.818.9 22.9 26 54.4 4.6 11.8 27.3 27 50.5 2.5 20.2 21.2 28 57.4 2.5 23.023.1 29 54.0 2.6 20.8 22.5 30 61.3 2.5 25.0 24.0 31 54.5 2.3 24.0 21.632 57.5 1.1 52.3 17.6 33 46.8 2.4 19.2 20.0 34 64.0 1.5 42.7 21.0 3559.8 1.9 31.5 21.7 36 60.4 1.7 36.6 20.8 37 54.7 5.1 10.7 28.4 38 59.62.3 25.9 23.0 39 60.1 3.6 16.7 26.9 40 53.8 2.4 22.4 21.8 41 63.0 1.737.1 21.6 42 57.1 1.9 30.1 21.0 43 59.8 2.3 26.0 23.1 44 68.0 2.4 28.325.5 45 67.4 2.2 30.8 24.6 46 65.9 2.1 32.2 23.7 47 69.1 3.8 18.3 30.048 64.1 0.8 84.3 16.7 49 60.3 2.6 23.2 24.2 50 70.8 1.7 41.6 23.4 5172.1 2.7 26.7 27.6 52 70.3 2.0 35.9 24.4 53 73.8 2.1 35.2 25.8 54 64.50.7 99.2 15.9 55 64.0 4.8 13.3 30.9 56 70.3 2.6 27.6 26.6 57 68.4 1.545.6 21.9 58 69.8 2.7 25.9 27.0 59 68.4 1.2 57.0 20.3 60 60.5 6.5 9.332.9 61 73.7 1.0 73.7 20.1 62 70.8 2.7 26.2 27.3 63 64.4 1.5 43.5 21.064 60.3 3.6 16.7 27.0 65 75.2 1.5 51.9 23.1 66 68.1 2.8 24.3 26.9 6763.4 3.6 17.6 27.9 68 68.2 3.3 20.7 28.4 69 78.5 3.1 25.3 30.6 70 61.02.0 31.3 22.2 71 68.8 1.1 62.6 19.8 72 72.1 2.4 30.0 26.5 73 74.7 1.745.3 24.0 74 69.3 3.2 21.6 28.5 75 80.1 2.3 34.8 28.1 76 76.3 1.9 40.125.5 77 66.1 2.1 31.5 24.0 78 83.0 1.0 83.0 21.8 79 76.7 2.0 39.3 25.880 71.8 2.2 32.6 25.7 81 76.5 1.4 56.6 22.8 82 73.2 2.5 29.5 27.1 8382.1 2.3 35.7 28.6 84 85.4 1.4 63.3 24.5 85 77.1 1.1 70.1 21.4 86 74.72.2 34.0 26.4 87 85.8 2.5 35.0 30.0 88 69.1 6.4 10.8 35.8 89 81.5 1.943.1 26.6 90 84.5 1.4 60.3 24.7 91 88.2 2.3 39.2 29.7 92 79.0 1.4 56.423.6 93 87.9 2.5 35.7 30.5 94 78.1 2.2 36.3 27.0 95 81.9 2.8 29.8 30.296 86.8 6.5 13.4 41.9 97 83.0 2.6 31.9 30.0 98 92.8 2.2 42.2 30.5 9988.7 2.1 42.2 29.2 100  64.2 3.2 20.1 27.1 101  77.3 2.1 36.7 26.7 102 77.6 1.2 64.7 22.1 103  89.7 1.4 64.0 25.7 104  87.5 1.4 62.5 25.2 105 94.7 2.5 37.9 32.3 106  85.0 1.3 68.0 23.8 107  79.1 1.2 68.8 22.1 108 90.8 1.4 64.9 25.9 109  85.4 1.4 63.3 24.5 110  67.4 0.7 96.3 16.8 111 86.6 1.7 50.9 26.7 112  84.2 2.3 36.6 29.0 113  78.4 2.1 37.3 26.9 114 100.8 2.3 44.6 32.5 115  86.9 2.7 32.2 31.3 116  96.2 1.5 66.3 27.2 117 93.1 2.1 44.4 30.1 118  89.8 2.4 37.4 30.7 119  93.3 2.1 44.4 30.1 120 98.4 3.4 28.9 36.7 121  99.9 2.7 37.0 34.3 122  84.0 2.2 38.2 28.6 123 92.6 1.1 84.2 24.2 124  95.8 1.4 68.4 26.8 125  107.9 3.0 36.0 37.4 126 94.7 2.7 35.1 33.1 127  94.4 1.6 59.0 27.8 128  88.4 2.6 34.0 31.2 129 89.4 0.9 99.3 22.1 130  101.1 1.5 67.4 28.4 131  80.4 2.0 40.2 26.9 132 107.1 1.4 76.5 28.9 133  102.5 3.9 26.3 39.5 134  101.6 1.7 59.7 29.7135  93.0 2.1 44.3 30.1 136  114.8 1.5 76.6 31.0 137  115.7 1.3 89.029.7 138  92.8 1.7 54.6 28.0 139  85.9 2.1 40.9 28.5 140  112.3 1.6 72.530.8 141  112.9 1.1 102.6 27.6 142  101.0 2.0 50.5 31.3 143  113.3 1.578.1 30.3 144  107.4 1.6 67.1 30.3 145  113.8 4.9 23.2 45.6 146  116.42.7 43.8 37.8 147  114.3 1.5 76.2 30.9 148  119.9 3.5 34.2 42.2 149 110.8 2.3 47.4 35.1 150  120.1 2.5 48.0 37.8 151  132.8 1.9 69.9 36.9152  100.5 3.2 31.4 36.5 153  135.5 2.0 67.8 38.1 154  121.1 1.3 93.230.6 155  142.1 1.8 78.9 37.9 156  133.7 1.7 78.7 35.7 157  125.5 1.396.5 31.3 158  146.8 4.3 34.1 51.8 159  145.3 2.1 69.2 40.5 160  151.92.1 72.3 41.7 161  160.0 2.7 59.3 47.0 162  148.9 1.9 78.4 39.8 163 156.7 5.8 27.0 59.8 164  156.3 1.2 130.3 35.3 165  151.8 1.5 101.2 37.3166  194.6 2.0 97.3 48.4 Average 80.9 2.3 42.6 27.3 St Dev 29.5 1.1 24.87.3

Atomic Force Microscopy (AFM) showed particles in the form of thinplatelets in a narrow size distribution (with approximately 85% of theparticles within 30 to 100 nm in the longest dimension). Of theplatelets measured: 6% of platelets were from about 31 nm to about 40 nmin diameter; 6% of platelets were from about 41 nm to about 50 nm indiameter; 13.3% of platelets were from about 51 nm to about 60 nm indiameter; 16.3% of platelets were from about 61 nm to about 70 nm indiameter; 14.5% of platelets were from about 71 nm to about 80 nm indiameter; 14.5% of platelets were from about 81 nm to about 90 nm indiameter; 8.4% of platelets were from about 91 nm to about 100 nm indiameter; 5.4% of platelets were from about 101 nm to about 110 nm indiameter; 6.6% of platelets were from about 111 nm to about 120 nm indiameter; 1.2% of platelets were from about 121 nm to about 130 nm indiameter; 1.8% of platelets were from about 131 nm to about 140 nm indiameter; 2.4% of platelets were from about 141 nm to about 150 nm indiameter; 3% of platelets were from about 151 nm to about 160 nm indiameter; and 0.6% of platelets were above 161 nm in diameter.

The AFM also showed particles with a narrow distribution of thicknesses(92% of particles were within 1 nm to 5 nm in thickness). Of theplatelets measured: 3% of platelets were from about 0.6 nm to about 1.0nm in thickness; 21.1% of platelets were from about 1.1 nm to about 1.5nm in thickness; 17.5% of platelets were from about 1.6 nm to about 2.0nm in thickness; 28.9% of platelets were from about 2.1 nm to about 2.5nm in thickness; 13.9% of platelets were from about 2.6 nm to about 3.0nm in thickness; 5.4% of platelets were from about 3.1 nm to about 3.5nm in thickness; 3% of platelets were from about 3.6 nm to about 4.0 nmin thickness; 0.6% of platelets were from about 4.1 nm to about 4.5 nmin thickness; 2.4% of platelets were from about 4.6 nm to about 5.0 nmin thickness; and 4.2% of platelets were over 5.1 nm in thickness.

Additionally, the AFM also showed particles with Equivalent SphericalDiameters (ESD) within a narrow size distribution (93% of particles hadan ESD within 15 nm to 40 nm). Of the platelets measured: 13.9% ofplatelets had an ESD from about about 11 nm to about 15 nm; 60.8% ofplatelets had an ESD from about 16 nm to about 20 nm; 19.9% of plateletshad an ESD from about 21 nm to about 25 nm; 19.9% of platelets had anESD from about 31 nm to about 40 nm; 4.2% of platelets had an ESD fromabout 41 nm to about 50 nm; and 1.2% of platelets had an ESD from about51 nm to about 60 nm.

The average BET surface area of this sample was determined to be 128.90m²/g. The BET surface area calculations are presented in Table 7. FIG. 6depicts the BET surface area plot. Comparison of the measured specificsurface area to a theoretical surface area of approximately 370 m2/g(for platelets 70 nm in diameter by 2.5 nm thick) gives good agreementwhile suggesting some platelet overlap in the measured sample. TABLE 7ABET Surface Area Report BET Surface Area 128.8966 +/− 0.2764 m2/g Slope0.033378 +/− 0.000071 g/cm3 STP Y-Intercept 0.000395 +/− 0.000014 g/cm3STP C 85.538723 Qm 29.6096 cm3/g STP Correlation Coefficient 0.9999795Molecular Cross-Sectional Area 0.1620 nm2

TABLE 7B Data for BET Surface Area Report Quantity Relative Absorbed(cm2/g Pressure (P/Po) STP) 1/[Q(Po/P − 1)] 0.048580010 25.7753 0.0019810.077168131 28.2181 0.002963 0.106361376 30.1089 0.003953 0.12337286831.0843 0.004528 0.147493213 32.4108 0.005338 0.172082949 33.76070.006157 0.196808435 35.1302 0.006975 0.221686588 36.5249 0.0077980.246587394 37.9562 0.008623 0.271375061 39.4484 0.009441 0.29617971841.0116 0.010261

The results of replicate zeta potential measurements are given in Table8. TABLE 8 Replicate Zeta Potential Measurements Zeta Potential ofMagnesium Hydroxide (mV) −1.9 −3.8 −4.2 −4.1 −5.2 −5.7 −4.1 −4.4 −4.4Average −4.2 Std Dev 1.0

The slurry was also tested using scanning electron microscope imagingand analysis by energy dispersive x-ray spectrometry. A portion of theslurry was diluted in isopropanol and a drop mount prepared on apolished carbon planchet. The prepared sample was mounted in a JEOL JSM6500F field emission scanning electron microscope equipped with a NoranVantage energy dispersive x-ray analysis system.

FIGS. 7 through 10 depict secondary electron images of typical particlesfrom the slurry. These particles were in the same size range (50-100 nm)and had the same morphology (thin platelets) as other Mg(OH)₂ samplespreviously examined. FIG. 11 is the EDS spectrum obtained from a portionof this sample, confirming the presence of magnesium (Mg) and oxygen(O), which is consistent with Mg(OH)₂, and is a result similar toanalyses of previous samples. (The large carbon peak in the spectrum isdue to the carbon substrate that supports the sample.)

A test was conducted to determine the effect of the system's flux onshape and size as compared to industrial product. Feed stock composed of1500 PPM of Mg²⁺ and 19,000 PPM of Cl⁻was diluted in an aqueous solutionat a pH of 4.1. The feedstock was passed through the electrolyzer at 80°F. (27° C.) and the pH was maintained at 11. The electrolyzer producedMg(OH)₂ that was washed by dilution at a rate of 10 to 1 and de-wateredthree times. The slurry was collected for analysis and furtherprocessing. Samples analyzed from the slurry were labeled Sample A. Aportion of the collected slurry was commercially spray dried under heat.The particles collected after this step were collected, analyzed, andlabeled Sample B. Sample A and B were compared to an industrial productused in provided by JM Huber, Inc., labeled Control.

A small portion of each sample was dispersed in deionized, particle-freewater, and a droplet placed on a polished carbon planchet and allowed todry. The dried samples were imaged in a JEOL JSM 6500F field emissionscanning electron microscope.

Comparison of the images of Sample A and Control showed very differentparticle morphologies. FIGS. 12A-H depict micrographs of Sample A. FIGS.13A-C depict micrograph images of the Control sample. FIGS. 14A-C depictmicrographs of Sample B. Comparison of the images of Sample A and theControl sample showed very different particle morphologies between thetwo samples. Sample A contained principally nanoplatelets with diametersup to a few hundred nanometers and thicknesses of only a few nanometers.In contrast, the Control sample consisted of blocky, roughly equalparticles with sizes down to tens of nanometers occurring asconglomerates of micrometer dimensions. Sample B appeared to be formedfrom aggregates of the nanoplatelets seen in Sample A, gathered andformed into rounded or ball-shaped particles of many micrometersdimension by drying a liquid droplet.

Nickel Hydroxide nanoplatelets doped with magnesium were prepared by themethod described above. Particularly, the center compartment of theelectrolyzer was filled with RO water containing NaCl at a concentrationof 75,000 ppm. The cathode and anode compartments were subsequentlyfilled with RO water containing NaCl at a concentration of 75,000 ppm.The pressure in the center compartment was maintained at a higher levelthan that of the anode and cathode compartments to keep the selectiveion membrane in place. The current in the machine was brought up to 7volts at 0.75 Amps/Square Inch. The temperature of the contents withinthe three compartments was maintained at about 110° F. (about 43° C.) ata pH of about 11. Feedstock was formulated with a final concentration ofCl⁻ ions at 30,000 ppm, Ni²⁺ ions at 1200 ppm, and Mg²⁺ ions at 300 ppm.The feedstock was fed through the center compartment at a rate of onegallon per minute, resulting in a residence time of 10 minutes. Materialwas collected in the catch basin and centrifuged. Slurry collected aftercentrifugation was tested to determine the characteristics of theparticles within the slurry. Table 9 depicts the quantitative resultsfor the nickel hydroxide nanoplatelets doped with magnesium. FIG. 15depicts the dispersive X-ray spectrum obtained from nickel hydroxidenanoparticles doped with magnesium within a slurry. FIG. 16A-C depictmicrograph images of nickel hydroxide nanoparticles doped withmagnesium. TABLE 9 Quantitative Results for Nickel Hydroxide Doped withMagnesium Element Weight % Weight % Error O 35.02 +/−1.71 Mg 22.68+/−0.81 Ni 42.3 +/−3.48 Total 100.0

Copper hydroxide nanoplatelets were prepared by the method describedabove. Particularly, the center compartment of the electrolyzer wasfilled with RO water containing NaCl at a concentration of 75,000 ppm.The cathode and anode compartments were subsequently filled with ROwater containing NaCl at a concentration of 75,000 ppm. The pressure inthe center compartment was maintained at a higher level than that of theanode and cathode compartments to keep the selective ion membrane inplace. The current in the machine was brought up to 7 volts at 0.75Amps/Square Inch. The temperature of the contents within the threecompartments was maintained at about 110° F. (about 43° C.) at a pH ofabout 11. Feedstock was formulated with a final concentration of Cl⁻ions at 30,000 ppm and Cu²⁺ ions at 1500 ppm. The feedstock was fedthrough the center compartment at a rate of one gallon per minute,resulting in a residence time of 10 minutes. Material was collected inthe catch basin and centrifuged. Slurry collected after centrifugationwas tested to determine the characteristics of the particles within theslurry. Table 10 depicts the quantitative results for the copperhydroxide nanoplatelets. FIG. 17 depicts the dispersive X-ray spectrumobtained from copper hydroxide nanoplatelets within a slurry. FIGS.18A-B depict micrographs of copper hydroxide nanoparticles within aslurry. TABLE 10 Quantitative Results for Copper Hydroxide Element NetCount Weight % Weight % Error O K 482 13.19 +/−1.81 Cu K 1266 86.81+/−5.90 Cu L 4057 — — Total 100.0Electrolyzer Configurations

In an alternative embodiment, a different electrolyzer configuration isemployed. The electrolyzer includes an anode compartment and a cathodecompartment as described above, but with a single ion selective membraneseparating the two compartments. NaCl is split in the anode chamber toyield chlorine gas and sodium ion, which passes through the membrane.Water is split in the cathode chamber to yield hydrogen gas and hydroxylion. A spacer in the cathode compartment separates the ion selectivemembrane from the cathode, creating a reaction area. Sodium chloride andmetal chloride are added to the cathode chamber. Metal ions react withhydroxyl ions in the cathode compartment to yield solid metal hydroxidein the cathode chamber leaving a free chloride which combines withsodium from the anode compartment to yield sodium chloride. As in thepreviously described method, metal hydroxide platelet size is determinedby adjusting selected variables, as described above. The residence timeof feedstock flow through the cathode compartment affects size (fasterflow rates result in smaller platelet size), and the quality of fluxline by the energy passing between the opposing compartments andtemperature affect the speed of reaction. As in the previous method, byadjusting these parameters, metal hydroxide platelets of uniform sizecan be produced. Tight size distributions can be obtained for plateletshaving an average platelet size of 3.5 microns in the X/Y plane and 100nm in the Z plane down to particles having an average particle size of30 nanometers in the X/Y plane and 2.5 nm in the Z plane. Generally, thefaster the platelets are harvested, the smaller the resulting platelets.The methods of preferred embodiments can be employed to preparenanoplatelets over a range of sizes, each having a narrow sizedistribution. Metal hydroxide nanoplatelets having an average plateletdiameter of from about 30 nm or less to about 1000, 1500, 2000, 2500, or3300, 3500 nm or more can be prepared, for example, from about 40, 50,60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, 180, or 190 nmto about 200, 250, 300, 350, 400, 450, 500, 600, 700, 800, or 900 nm.Particularly preferred are nanoplatelets having an average plateletdiameter of about 40, 50, or 60 nm to about 70, 80, 90, 100, 110, or 120nm.

The metal hydroxide nanoplatelets of preferred embodiments can beconverted into metal oxide-containing nanoplatelets or metaloxide-containing nanotubes. In a preferred conversion method forpreparing metal oxide-containing nanoplatelets, metal hydroxidenanoplatelets are heated uniformly, for example., in an oven, at atemperature sufficient to dehydrate the metal hydroxide. Any suitablemethod for heating can be employed, for example convection heating, aradiant heat source, contact heating, or the like. The temperature andexposure time can be adjusted such that different degrees of conversionof metal hydroxide to metal oxide in the nanoplatelets can be achieved(e.g., less than 1% conversion of metal hydroxide or more than 99%conversion of metal hydroxide). Metal oxide containing nanotubes can beprepared by non-uniform heating (e.g., by applying heat to one side of ametal hydroxide nanoplatelet). Non-uniform heating can be conducted by,e.g., use of a heat lamp or a hot plate to apply heat preferentially toone side of a metal hydroxide nanoplatelet. Metal hydroxide on theheated side undergoes conversion to metal oxide at a faster rate thanthe opposite side, resulting in the formation of stresses in thenanoplatelet that are relieved by curling of the nanoplatelet into atubular structure. The resulting metal oxide containing nanotubes can beuseful in applications similar to those in which metal hydroxidenanoplatelets or metal oxide nanoplatelets are used. Nanotubes of thepreferred embodiments have potential applications in electronics, opticsand other fields of materials science and the diameter of the nanotubedepend upon the base platelet size used for the varying applications.

Decontamination of Chemical and Biological Agents

The metal hydroxides and metal oxides of preferred embodiments aresuitable for use in a variety of applications. In a particularlypreferred embodiment, the metal hydroxides and metal oxides are usefulfor decontamination of chemical and biological agents. Chemical andbiological weapons pose a serious threat to both civilians and militarypersonnel. Detection and neutralization of chemical and biologicalagents is of great interest to both. An urgent need exists fordeveloping simple and cost effective techniques that can be used forneutralizing chemical and biological agents. A liquid free process notharmful to humans, the environment or equipment is preferred. Presently,different ways of neutralizing chemical and/or biological-agentcontamination exist. All suffer from various disadvantages. Chemicaldecontamination of chemical and/or biological agents often utilizes sometype of hypochlorite solution. Hypochlorites are very corrosive andharmful to skin. Certain materials, particularly electronic and avionic,can suffer serious damage during neutralization by solution-basedtechniques due to corrosive chemical reactions.

Solution based techniques for decontamination are not suitable forexpensive electronic and avionic equipment. Other disadvantages ofsolution based decontamination include environmental pollution, thetransport and storage of corrosive chemicals, and health risks. Theproblems associated with chemical decontamination can be overcome byusing physical decontamination techniques. An example of this isutilization of UV light, combined with a cost effective, inert materialexhibiting exceptional adhesion and capable of producing free radicalswith high efficiency.

Mg(OH)₂ and MgO in the shape of nanoplatelets have unique chemical andphysical properties. Nanoplatelets of Mg(OH)₂ and MgO offer simple andcost effective ways of neutralizing chemical and/or biological agents.This is especially true for electronic and avionic equipment. TheMg(OH)₂ used for this application is preferably in the form ofindividual crystallites of 30-100 nm in length and width with athickness of only a few nanometers. The unique structure of the Mg(OH)₂nanoplatelets provides much higher specific surface area thanthree-dimensional nanoparticles. This higher specific surface areaprovides great driving force for diffusion, especially at elevatedtemperatures. Further, the higher specific surface area allows sinteringto take place at lower temperatures, over shorter time scales.Additionally, the higher specific surface area of the nanoplatelets alsoreduces the incipient melting temperature. Even with the higher specificsurface area, it is recognized in the art that the density of the finalproduct is unaffected. In addition these nanoplatelets have excellentadhesion properties due to their geometric shape and can be applied tocontaminated surfaces in dry form. The nanoplatelets' chemicalreactivity is greatly enhanced due to the surface to volume ratioincrease. Nanoplatelets have a much higher surface area thannanoparticles. Dehydration at high temperature converts the Mg(OH)₂ intoMgO. The nanoplatelets of MgO have a porous surface morphology whichfurther increases the surface area of the nanoplatelets.

In addition to the generic effect of high surface area of nanoplateletsas opposed to conventional nanoparticles, the nanoplatelets of Mg(OH)₂are a very strong base and therefore possess antimicrobial propertieswhich can be exploited for neutralizing biowarfare agents. While thehigh efficiency destructive adsorption of biological materials by oxidenanoparticles has been reported in the literature, nanoplatelets canexhibit a substantial increase in adsorption and reactivity over suchconventional nanoparticles.

Nanoplatelets can be used as decontamination agents in passive or activemodes. Both modes require dispersion of nanoplatelets onto contaminatedsurfaces in a dry from using dry spraying/dusting techniques. Thesenanoplatelets adhere to surfaces by van der Walls forces due to theirlarge surface to volume ratio. Both of these methods do not use anysolutions or water for decontamination. The passive mode ofdecontamination exploits the formation of monolayers of water aroundnanoparticles due to capillary condensation. Individual nanoplatelets ofMg(OH)₂ on a surface form a water meniscus around their surfaces atordinary humidity, due to capillary condensation. Even in dryconditions, a thin layer of water condenses around nanoparticles. Atordinary humidity, many monolayers of water condense on these surfaces.Even at 10-20% relative humidity a few layers of water form on edgesfrom capillary condensation due to extremely small radius of curvatureof the edges. The water meniscus, which forms immediately around thenanoplatelets' surfaces, destroys the chemical and/or biological warfareagents on contact. Due to the highly basic nature of the water meniscus,nanoplatelets of Mg(OH)₂ can neutralize harmful chemical and/orbiological warfare agents, proteins, biotoxins, and even spores withoutdamaging the surface. The combination of the chemical (strong base watermeniscus) and structure (extremely high surface areas, rich morphologydefects, with sharp edges, tips and nanocrystallite sizes) results inextremely high chemical reactivity including enhanced reaction kineticswith large capacities. Chemical and/or biological agents contacting thenanoplatelets are chemically destroyed without the use of solutions.

In the active mode of decontamination, these nanoplatelets can be usedto create free radicals to destroy chemical and/or biological agents.These MgO nanoplatelets have wide electronic band gaps. Illumination ofnanoplatelets with ultra violet (UV) light results in electron-hole pairformation. The geometrical shape of nanoplatelets results in electronicband bending due to surface defects. The UV created electron-hole pairsare separated from the field and create free radicals. These freeradicals destroy chemical and biological material in the vicinity of thenanoplatelets. Due to their shape, the nanoplatelets have betteradsorption properties than spherical nanoparticles of the same volume.By controlling the size of the nanoplatelet, it can be tuned to specificUV wavelength for optimization of free radical creation. The efficacy ofMg(OH)₂ and MgO as neutralizing agents for chemical and biologicalagents can be enhanced by modifying their surfaces with halogens. Sincethese are nanoplatelets rather than spherical particles, the edges areexpected to have higher chemical activities. A schematic diagramdepicting a decontamination process is provided in FIG. 19.

Selected metal hydroxide nanoplatelets of preferred embodiments offeradvantages in decontaminating chemical and/or biological agents,including a large surface to volume ratio and high adhesion properties;easy to disperse as dry powder; ideal for electronic and avionicequipment (can be decontaminated in place); localized neutralization ofchemical and/or biological agents on contact; solution freedecontamination; passive mode of decontamination exploiting naturalhumidity; and the magnesium hydroxide nanoplatelets in the active modeof decontamination using UV-generated free radicals; platelet size canbe tuned for maximization of free radical creation; both passive andactive modes can be carried out simultaneously.

Papermaking

In one particularly preferred embodiment, the metal hydroxides and metaloxides are useful in papermaking. In papermaking, retention is definedin general as the process of keeping fine particles and fiber fineswithin the web of paper as it is being formed. It is important to havegood retention for the efficiency of the papermaking operation. Lowretention can lead to many problems, including: poor runnability,increased deposits, sheet defects, higher additive costs, more downtimefor washups, and higher sewer losses. Thus, retention aids can improvethe overall runnability of the papermaking machine, and allow increasesin speed through better drainage. In addition, retention can reducedeposits and sheet breaks caused by high levels of fillers and finescirculating at the wet end, and reduce furnish costs through better useof fillers or other additives.

The demand for retention aids has increased as papermakers seek to makealkaline rather than acid paper, incorporate higher levels of fillers,operate the paper machines at higher speeds, increase the extent ofclosure of the white water system and increase the use of recycledfibers. An effective retention program can enable the papermaker tooptimize sizing efficiency, good opacity, efficiency in the overallmachine runnability, and reduce furnish costs through better utilizationof fillers or other additives. A good retention program can also helpthe papermaker achieve desired sheet qualities by optimizing theretention of expensive additives such as titanium dioxide, wet and drystrength additives, and alkaline size.

Conventional types of retention/drainage aids include inorganic salts,natural polymers and synthetic polymers. Examples of the inorganic saltsare alum, silicas and bentonite clays. Cationic starch is the mostcommonly employed retention aid based on natural polymers. The syntheticpolymers include structures based on polyacrylamides, polyamines,polyethyleneimine, polyamidoamines, and polyethlene oxide.

Retention and drainage aid programs have evolved from the use of asingle flocculant or conventional coagulant to flocculant programs thatinclude the use of anionic nanoparticles based on bentonite clays orsilicas. These anionic nanoparticles have been used along with cationicstarches, coagulants, and polyacrylamide-based flocculants to achievehigher benchmarks for retention, drainage, and formation. Nanoparticletechnologies can improve retention, drainage, and formation.Nanoparticle systems have significant advantages over conventionalsingle and dual polymer retention systems, due to the small, tightflocculant forms which adsorb strongly to the furnish components,leaving the sheet structure open and uniform. Advantages of nanoparticlesystems include increased retention and drainage with no sacrifice information, and better performance in the presence of high concentrationsof interfering substances. The nanoparticle retention system permits theclean-up of the white water loop by effectively retaining the suspendedand dissolved solids including fillers with wood fibers.

Nanoparticles used for retention and drainage promotion arecharacterized by high surface area and negative charge. There are twocommercially available nanoparticles in use today: colloidal silica andcolloidal bentonite Papermakers utilize colloidal silica worldwide andrelated products each year to promote dewatering and fine-particleretention on hundreds of paper machines during production of over tenmillion annual tons of paper and paperboard products. Bentonite is asecond type of mineral additive used in combination with cationicpolymers for retention and drainage enhancement; and sometimes also forpitch control.

For all nanoparticle systems, the basic mechanism is the same. Itinvolves interactions with all three fundamental mechanisms includingcoagulation, flocculation, and lastly the formation of the nano floc.This is based upon the three fundamental mechanisms: chargeneutralization, bridging, and patching. In a preferred embodiment, lowmolecular weight high charge polymers can be used in the coagulationmechanism to control the wet end chemistry balance. With flocculation,bridging flocculation is induced, resulting in large flocs that arebroken down under applied shear. Nanoplatelets of the preferredembodiments can be used in microflocculation. In a preferred embodiment,anionic nanoplatelets of the preferred embodiments can provide negativesites that can interact with the positively charged flocs to form ahighly coagulated system of hare dense, small flocs that readilydewater. Accordingly, nanoplatelets of the preferred embodiment canprovide high retention, superior formation and superior drainage whencompared to conventional systems.

Fire Retardants

The nanoparticles of the preferred embodiments can be employed to impartfire retardancy to various materials (e.g., polymer-containing paints,fibers, coatings, and the like).

Poly(trimethylene terephthalate), also called poly(propyleneterephthalate) (PPT), belongs to the thermoplastic aromatic polyesterfamily, which includes poly(ethylene terephthalate) (PET) andpoly(butylenes terephthalate) (PBT). PTT fibers were developed in 1990sand are considered to be important fibers since PTT fibers combine thebest properties of polyamide and polyester for unique comfort andstretch. The key advantage is that it combines the desirable physicalproperties of PET (strength, stiffness and toughness), while retainingbasic polyester benefits of dimensional stability, electricalinsulation, and chemical resistance. PTT fibers provide a luxuriousfeel, inherent stain resistance, excellent dyeability, antistaticproperties, and easy care. Because of the unique mechanical propertiesand its lower melting temperature, PTT has better processing abilitythan other aromatic polyester, such as PET. These advantages make itpossible to use PTT as carpets and clothing materials. In carpetapplications, PTT's excellent crush resistance, static resistance,colorfastness, and stain resistance making PTT the better choice in manycarpet applications.

Although PTT fibers have excellent physical, mechanical and comfortproperties, the relatively poor fire retardant ability, particularlyunder radiant panel test conditions as compared with nylon, limits theapplication of PTT fibers in carpet application.

Nanoplatelets of preferred embodiments can contribute to improving fireretardancy. Magnesium hydroxide in Nanoplatelets decomposesendothermically when heated to yield magnesium oxide nanoplatelets(MgO), a thermal insulator and water. The water acts to smother theflame by diluting and/or excluding oxygen and flammable gases, and theheat insulating nanoplatelets congregate on and in the surface area ofcertain polymeric materials containing such nanoplatelets when incontact with the flame, reducing or preventing the availability ofpotentially flammable decomposition products below the surface area toconvert to the gas phase where combustion occurs.

Many other inorganic particles such as TiO₂, Al(OH)₃, Mg(OH)₂, andsilicates have been used to improve the fire retardancy of polymers.However, extremely high loading exceeding 30 wt. % of inorganic mineralparticles is typically needed to achieve satisfactory anti-flammability.This greatly impedes potential applications in carpet and textile. Thisobstacle is avoided with nanoplatelets of the preferred embodiments. Theincrease in barrier properties associated with nanoplatelets of thepreferred embodiments obviates the need for such high loading.

As smaller load sizes can achieve a reduction in heat release, theobstacles faced by the larger nanoclays in potential applications suchas carpet and textiles are not an issue with the nanoplatelets of thepreferred embodiments.

Unlike mechanically reduced nanoparticles, the nanoparticles of thepreferred embodiments can be supplied as a suspension of isolatednanoplatelets and as such have potential applications as fire retardantsin carpet and textiles. Nanoparticles of any metal potentially haveapplications as fire retardants in carpet and textiles. In an especiallypreferred embodiment, the plate thickness is about 1 nm to about 10 nmas shown in FIG. 20. In a preferred embodiment, Al(OH)₃ can be used as afire retardant. In an especially preferred embodiment, Mg(OH)₂nanoplatelets can be used as a fire retardant. Because Mg(OH)₂ by itselfis an effective fire retardant additive for polymers, the availabilityof such nanoplatelets can enable potential fire retardant applicationswith considerably low filler loadings. The nanoparticles of thepreferred embodiments can be used to provide remarkably improved fireretardancies when added to various fibers and polymers where improvedfire retardancy is desirable

Various approaches can be employed to incorporate nanoplatelets of thepreferred embodiments into PTT. For example, a master batch of PTT withnanoplatelets of the preferred embodiments can be prepared, and thenblended with virgin PTT in the fiber extrusion line. Alternatively,nanoplatelets of the preferred embodiment can be suspended in any fluidsuitable for suspension, for example, the nanoplatelets can be suspendedin water. Also, direct mixing of polyester emulsion with thenanoplatelet suspension can be used to make a master batch of PTT withnanoplatelets. Alternatively, the nanoplatelet suspension can be mixedwith other suitable polymers.

In another preferred embodiment, nanoplatelets of the preferredembodiments are dispersed in a carrier polymer directly from thenanoplatelet water suspension. Surprisingly, nanoplatelets (e.g.,Mg(OH)₂) can be dispersed in polystyrene latex to form a well dispersednanocomposite. A carrier polymer, such as polyester, that has strongaffinity with PTT can be employed.

In yet another preferred embodiment, dry nanoplatelets are directlyblended with PTT in the fiber extrusion line.

Similar approaches can be employed to provide fire retardancy for otherpolymers that can benefit from fire retardancy, for example polymerssuch as polyester, aramid fiber (e.g., Twaron), acrylic, nylon, spandex(trade name Lycra), olefin, ingeo, and lurex, and other polymers as arecommonly employed in fabricating carpets, drapes, wall coverings, foamcushions, mattresses, carpet padding, blinds, paints, varnishes, floorcoverings (e.g., Pergo, formica, linoleum, vinyl), clothing (e.g.,infant clothing), and the like.

Improving Materials' Strength

In yet another embodiment, the nanoplatelets of the preferredembodiments can be employed to produce lightweight body armor materials.In other embodiments, nanoplatelets of the preferred embodiments can beused in applications where enhanced strength is useful, for example inaromatic polyamides such as Twaron, Kevlar and Nomex. Nanoplatelets ofthe preferred embodiments can be added to the polymers usingconventional methods typically employed to add solid fillers topolymeric materials.

Nanoplatelets of the preferred embodiments can be used in theconstruction of an intricate alternatively layered organic/inorganichybrid composite designed to combine ceramic's hardness and polymer'stoughness, to replace or partially replace the current commerciallyavailable armor materials.

Armor materials, with light weight and high strength, are in an everincreasing demand in facing the terrorist threat and future battle fieldrequirement. Among those, the SiC and BN₄ have been two typicalexamples, and have been widely used in soldier protection. However, therelative heavy weight and more than one inch's thickness inanti-ballistic protection are still two hurdles to be overcome. Flexiblearmor materials, e.g., the well known Kevlar and ultrahigh polyethylenematerials, in contrary, has problems of supplementing hard matrix interms of withstanding the ballistic attack, although they both possessexcellent comprehensive mechanical properties. Therefore, it has becomeimperative to develop new generation armors that have comparativehardness and flexuralability with SiC or BN₄but with the specific weightof artificial polymers such as Kevlar.

One way to increase the mechanical strength of a surface is byincorporating hard nanoplatelets materials. Alternating layers ofnanoplatelets and soft adhesive material can increase the strength thematerial many fold. The alternating layers of orientated hard materialsand soft materials have large interface area that can absorb anddissipate energy compared to ordinary materials

Nanoplatelets of the preferred embodiments can be used to increase thestrength of a surface. When the nanoplatelets are magnetic, a singlelayer of nanoplatelets can be deposited on a surface usingspin/dip-coating under a magnetic field. In a preferred embodiment,coating techniques are carried out in a magnetic field for aligning theplates on the surface. The magnetic field orients the plates parallel tothe substrate. To produce magnetic nanoparticles, the (hydr)oxides arefirst converted to the corresponding metal. This can be accomplished byconventional reduction reactions known in the art. For example, Ninanoplatelets can be prepared through the Ni²⁺ reduction reaction byhydrazine hydrate in a 40 kHz ultrasonic irradiation reaction, asdescribed in Li et al., Nanotechnology 15 (2004) 982-986, hereinincorporated by reference in its entirety. The pH value is preferablymaintained at 14 using NaOH solution. After the mixed aqueous solutioncontaining NiCl₂, preferably a nickel (hydr)oxide, and hydrazine hydrateare put into the ultrasonic bath, the solution color gradually changesfrom green to grey black. When the solution turns completely black, thereduction reaction is complete Spin coating of polystyrene spheres formwell ordered layers on substrates. A thin layer of polymer is depositedon the nanoplatelet layer. Any suitable polymeric material can be used,for example polyethylene, polypropylene, polyvinyl chloride,polyethylene terephthalate, polystyrene and polycarbonate. Subsequentalternating layers of nanoplatelets and polymer are deposited until therequired overall thickness is reached.

Magnetic nanoparticles of the preferred embodiment can be incorporatedinto data-carrying devices, including but not limited to, computermemory devices, hard drives, digital media, and portable memory.

To build a light-weight and high strength material for body armorapplication, an external pressure can be applied to help the alignmentof randomly dispersed nanoplatelets in the presence of polymer bondingagent, as shown in FIG. 21. The different polymers, polymer/nanoplateratio, temperature, pressure, solid contents during compression, andnanoparticles can be tested.

To build a light-weight and high strength material for body armorapplication, positively and negatively charged thin layer (approximately1.0 μm mimicking the thickness of nature nacre) of nanoplatelet Mg(OH)₂polymer matrix can be constructed following the Langmuir-Blodgettconcept, and transferred alternatively one atop another andself-assembled to form the target layered structure, as shown in FIG.22. An external pressure can optionally be applied

To build a light-weight and high strength material for body armor, amulti-layer nature nacre structure can be constructed by alayer-by-layer method using alternatively dipping in oppositely chargednanoplatelet Mg(OH)₂/polymer binder solution, as shown in FIG. 23. Alongthe layer-by-layer dipping process, the surface charge will be changedalternatively, as shown in the plot

To build a light-weight and high strength material for body armor,magnesium hydroxide nanoplatelets and polyethylene glycol can be used tomake shear thickening fluids to be used in making liquid body armor(FIG. 24).

Plasmonics

The nanoparticles of the preferred embodiments can also be used as abases for plasmonics. Plasmonics is a technique for transmitting opticalsignals along minuscule nanoscale structures. Directing light waves atthe interface between a nanometal coated dielectric material can inducea resonant interaction between the waves and the mobile electrons at thesurface of the metal. The result is the generation of surfaceplasmons—density waves of electrons that propagate along the interface.Plasmon-carrying nanoplatelets of the preferred embodiment can beincorporated into various devices, including, but not limited to,microscopes, light-emitting diodes (LEDs), as well as chemical andbiological sensors. Plasmons of the preferred embodiment can also beincorporated into data-carrying integrated circuits with electricalinterconnects.

In one embodiment, the nanoplatelets of the preferred embodiments areincorporated into a plasmonic device through placement in a reducingenvironment with reducing gas. The top layer of the particular metalhydr(oxide) can be converted to its elemental form encapsulating theunderlying hydroxide or oxide material, a dielectric material, of thatbase nanoplatelet.

Methods and devices that are suitable for use in conjunction withaspects of the preferred embodiments are disclosed in: U.S. Pat. No.5,264,097, entitled “ELECTRODIALYTIC CONVERSION OF COMPLEXRES AND SALTSOF METAL CATIONS,” U.S. Pat. No. 3,959,095; entitled “METHODS OFOPERATING A THREE COMPARTMENT ELECTROLYTIC CELL FOR THE PRODUCTION OFALKALLI METAL HYDROXIDES;” U.S. Publication No. 20070022839, entitled“SYNTHESES AND APPLICATIONS OF NANO-SIZED IRON PARTICLES;” U.S. Pat. No.7,172,747, entitled “METAL OXIDE NANOTUBE AND PROCESS FOR PRODUCTIONTHEREOF;” U.S. Pat. No. 6,656,339, entitled “METHOD OF FORMING ANANO-SUPPORTED CATALYST ON A SUBSTRATE FOR NANOTUBE GROWTH;” U.S. Pat.No. 5,470,910, entitled “COMPOSITE MATERIALS CONTAINING NANOSCALARPARTICLES, PROCESS FOR PRODUCING THEM AND THEIR USE FOR OPTICALCOMPONENTS;” U.S. Publication No. 20070098806, entitled “POLYMER-BASEDANTIMICROBIAL AGENTS, METHODS OF MAKING SAID AGENTS, AND PRODUCTSINCORPORATING SAID AGENTS;” U.S. Publication No. 20060216602, entitled“MACROSCOPIC ASSEMBLY OF NANOMETRIC FILAMENTARY STRUCTURES AND METHOD OFPREPARATION THEREOF;” U.S. Publication No. 20060193766, entitled“TITANIA NANOTUBE AND METHOD FOR PRODUCING SAME;” U.S. Publication No.20060159603, entitled “SEPARATION OF METAL NANOPARTICLES;” Boo et al.,Fracture Behavior of Nanoplatelet Reinforced Polymer Nanocomposites,Mat. Sci. and Tech. 22(7) 2006: 829-834; Li et al., Structure andMagnetic Properties of Cobalt Nanoplatelets, Mat. Lett. 58 (2004):2506-2509; Zhou et al., Preparation and Characterization ofNanoplatelets of Nickel Hydroxide and Nickel Oxide, Mat. Chem. and Phys.98(2006): 267-272; Sun et al., From Layered Double Hydroxide to SpinelNanostructures: Facile Synthesis and Characterization of Nanoplateletsand Nanorods, J. Phys. Chem. B. 110 (2006): 13375-13380; Zarate et al.,Novel Route to Synthesize CuO Nanoplatelets, J. Sol. St. Chem.180(2007): 1464-1469; Shouzhu et al., Nanofibers and Nanoplatelets ofMoO ₃ via an Electrospinning Technique, J. Phys. and Chem. Of Sol.67(2006): 1869-1872; Hou et al., High-Yield Preparation of UniformCobalt Hydroxide and Oxide Nanoplatelets and Their Characterization, J.Phys. Chem. B. 109(2005): 19094-19098; and Liu et al., Facile andLarge-Scale Production of ZnO/Zn—Al Layered Double HydroxideHierarchical Heterostructures, J. Phys. Chem B. 110(2006): 21865-21872.

All references cited herein, including but not limited to published andunpublished applications, patents, and literature references, andreferences in the Appendix, are incorporated herein by reference intheir entirety and are hereby made a part of this specification. To theextent publications and patents or patent applications incorporated byreference contradict the disclosure contained in the specification, thespecification is intended to supersede and/or take precedence over anysuch contradictory material.

The term “comprising” as used herein is synonymous with “including,”“containing,” or “characterized by,” and is inclusive or open-ended anddoes not exclude additional, unrecited elements or method steps.

All numbers expressing quantities of ingredients, reaction conditions,and so forth used in the specification are to be understood as beingmodified in all instances by the term “about.” Accordingly, unlessindicated to the contrary, the numerical parameters set forth herein areapproximations that may vary depending upon the desired propertiessought to be obtained. At the very least, and not as an attempt to limitthe application of the doctrine of equivalents to the scope of anyclaims in any application claiming priority to the present application,each numerical parameter should be construed in light of the number ofsignificant digits and ordinary rounding approaches.

The above description discloses several methods and materials of thepresent invention. This invention is susceptible to modifications in themethods and materials, as well as alterations in the fabrication methodsand equipment. Such modifications will become apparent to those skilledin the art from a consideration of this disclosure or practice of theinvention disclosed herein. Consequently, it is not intended that thisinvention be limited to the specific embodiments disclosed herein, butthat it cover all modifications and alternatives coming within the truescope and spirit of the invention.

1. Metal hydroxide nanoplatelets having an average platelet diameter offrom about 30 nm to about 3500 nm and an average thickness of from about1 nm to about 400 nm.
 2. Metal hydroxide nanoplatelets of claim 1,having an average platelet diameter of from about 40 nm to about 120 nmand an average thickness of from about 1 nm to about 4 nm.
 3. Metalhydroxide nanoplatelets of claim 1, having an average aspect ratio offrom about 15 to about 70, an average BET specific surface area of fromabout 100 m²/g to about 150 m²/g, and an average zeta potential of fromabout +60 mV to about −60 mV.
 4. Metal hydroxide nanoplatelets of claim1, having an average aspect ratio of from about 15 to about 70, anaverage BET specific surface area of from about 100 m²/g to about 150m²/g, and an average zeta potential of from about −4 mV to about −5 mV.5. Metal hydroxide nanoplatelets of claim 1, selected from the groupconsisting of Mg(OH)₂, Ca(OH)₂, Al(OH)₃, Sr(OH)₂, Ba(OH)₂, Fe(OH)₃,Cu(OH)₂, Ni(OH)₂, Co(OH)₂, Zn(OH)₂, AgOH, and mixtures thereof.
 6. Metalhydroxide nanoplatelets of claim 1, further comprising at least onemetal oxide.
 7. Metal hydroxide nanoplatelets of claim 6, wherein themetal oxide is selected from the group consisting of MgO, SrO, BaO, CaO,TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO, Ni₂O₃, CuO, Al₂O₃, SiO₂,ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂], and mixtures thereof.
 8. Metal hydroxidenanoplatelets of claim 1, in a form of rolled nanotubes.
 9. Metal oxidenanoplatelets having an average platelet diameter of from about 30 nm toabout 3500 nm and an average thickness of from about 1 nm to about 400nm.
 10. Metal oxide nanoplatelets of claim 9, having an average plateletdiameter of from about 40 nm to about 120 nm and an average thickness offrom about 1 nm to about 4 nm.
 11. Metal oxide nanoplatelets of claim 9,having an average aspect ratio of from about 15 to about 70, an averageBET specific surface area of from about 100 m²/g to about 150 m²/g, andan average zeta potential of from about +60 mV to about −60 mV. 12.Metal oxide nanoplatelets of claim 9, selected from the group consistingof MgO, SrO, BaO, CaO, TiO₂, ZrO₂, FeO, V₂O₃, V₂O₅, Mn₂O₃, Fe₂O₃, NiO,Ni₂O₃, CuO, Al₂O₃, SiO₂, ZnO, Ag₂O, [Ce(NO₃)₃—Cu(NO₃)₂]TiO₂, andmixtures thereof.
 13. A method of producing metal hydroxidenanoplatelets, comprising the steps of: providing an electrolyzercomprising an anode compartment, a cathode compartment, and a centercompartment situated between the anode compartment and the cathodecompartment, and separated from the anode compartment and the cathodecompartment by ion selective membranes; adding a solution of electrolyteat a pH of about 8 to the anode compartment; adding a solution of up toabout 50 wt. % sodium hydroxide at a pH of 8 or higher to the cathodecompartment; adding a solution of a second electrolyte to the centercompartment, wherein the solution has from about 30,000 ppm chloride ionto about 200,000 ppm chloride ion; operating the cathode compartment atan amperage of 3.75 amps per square inch or less, whereby hydroxide ionis generated in the cathode compartment and migrates through its ionselective membrane into the center compartment, and whereby sodium ionis generated in the anode compartment and migrates through its ionselective membrane into the center compartment; and thereafter adding tothe center compartment a solution of soluble metal ion and a thirdelectrolyte, the solution having from about 300 ppm to 100,000 ppm metalions and from about 5000 ppm to about 200,000 ppm anions, whereby thesoluble metal ion reacts with hydroxide ion to yield metal hydroxidenanoplatelets, wherein a residence time in the center compartment of themetal hydroxide nanoplatelets is from about 0.1 minutes to about 10minutes.
 14. The method of claim 13, wherein the soluble metal ion isselected from the group consisting of magnesium ion, strontium ion,barium ion, calcium ion, titanium ion, zirconium ion, iron ion, vanadiumion, manganese ion, nickel ion, copper ion, aluminum ion, cobalt ion,silicon ion, zinc ion, silver ion, cerium ion, and mixtures thereof. 15.The method of claim 13, wherein the solution comprises water.
 16. Themethod of claim 13, wherein the solution of soluble metal ion and anelectrolyte is adjusted to a pH of 4.5 or less, whereby carbonates areremoved from the solution.
 17. The method of claim 13, wherein thesolution of soluble metal ion and an electrolyte is added to the centercompartment at a temperature of from about 60° F. to about 190° F. 18.The method of claim 13, further comprising the step of removing residualwater from the metal hydroxide nanoplatelets, whereby dried metalhydroxide nanoplatelets are obtained.
 19. The method of claim 18,further comprising the step of applying heat to one side of the driedmetal hydroxide nanoplatelets, whereby metal hydroxide is converted tometal oxide through a portion of a thickness of the nanoplatelets,causing them to roll into nanotubes, whereby metal (hydr)oxide nanotubesare obtained.
 20. The method of claim 18, further comprising the step ofapplying heat to the dried metal hydroxide nanoplatelets, whereby metalhydroxide is converted to metal oxide through the thickness of thenanoplatelets, whereby metal oxide nanoplatelets are obtained.
 21. Themethod of claim 13, wherein the metal hydroxide nanoplatelets have anaverage platelet diameter of from about 30 nm to about 3500 nm and anaverage thickness of from about 1 nm to about 400 nm.
 22. The method ofclaim 13, wherein the metal hydroxide nanoplatelets have an averageplatelet diameter of from about 40 nm to about 120 nm and an averagethickness of from about 1 nm to about 4 nm.
 23. The method of claim 13,wherein the first, second, and third electrolyte is sodium chloride.